Composition for heat cycle system, and heat cycle system

ABSTRACT

A composition for a heat cycle system having favorable lubricating properties is provided. A heat cycle system employing the composition is also provided. The composition contains a working fluid for heat cycle, which has a low global warming potential and can replace R410A. The working fluid contains an unsaturated fluorinated hydrocarbon compound having a specific structure and a refrigerant oil having a breakdown voltage of at least 25 kV, a hydroxy value of at most 0.1 mgKOH/g, and a minimum temperature on the high temperature side of the phase separation temperature from the working fluid of at least 35° C. and a maximum temperature on the low temperature side of at most −60° C.

TECHNICAL FIELD

The present invention relates to a composition for a heat cycle system,and a heat cycle system employing the composition.

BACKGROUND ART

In this specification, abbreviated names of halogenated hydrocarboncompounds are described in brackets after the compound names, and inthis specification, the abbreviated names are employed instead of thecompound names as the case requires.

Heretofore, as a working fluid for a heat cycle system such as arefrigerant for a refrigerator, a refrigerant for an air-conditioningapparatus, a working fluid for power generation system (such as exhaustheat recovery power generation), a working fluid for a latent heattransport apparatus (such as a heat pipe) or a secondary cooling fluid,a chlorofluorocarbon (CFC) such as chlorotrifluoromethane ordichlorodifluoromethane or a hydrochlorofluorocarbon (HCFC) such aschlorodifluoromethane has been used. However, influences of CFCs andHCFCs over the ozone layer in the stratosphere have been pointed out,and their use is regulated at present.

Under the above conditions, as a working fluid for a heat cycle system,a hydrofluorocarbon (HFC) which has less influence over the ozone layer,such as difluoromethane (HFC-32), tetrafluoroethane or pentafluoroethane(HFC-125) has been used, instead of CFCs and HCFCs. For example, R410A(a pseudoazeotropic mixture of HFC-32 and HFC-125 in a mass ratio of1:1) is a refrigerant which has been widely used. However, it is pointedout that HFCs may cause global warming.

R410A has been widely used for a common air-conditioning apparatus suchas a so-called package air-conditioner or room air-conditioner, due toits high refrigerating capacity. However, it has a global warmingpotential (GWP) of so high as 2,088, and accordingly development of aworking fluid with low GWP has been desired. Further, development of aworking fluid has been desired on the condition that R410A is simplyreplaced and existing apparatus will be used as they are.

In recent years, a hydrofluoroolefin (HFO) i.e. a HFC having acarbon-carbon double bond is expected, which is a working fluid havingless influence over the ozone layer and having less influence overglobal warming, since the carbon-carbon double bond is likely to bedecomposed by OH radicals in the air. In this specification, a saturatedHFC will be referred to as a HFC and distinguished from a HFO unlessotherwise specified. Further, a HFC may be referred to as a saturatedhydrofluorocarbon in some cases.

As a working fluid employing a HFO, for example, Patent Document 1discloses a technique relating to a working fluid usingtrifluoroethylene (HFO-1123) which has the above properties and withwhich excellent cycle performance will be obtained. Further, PatentDocument 2 discloses a technique relating to a working fluid using1,2-difluoroethylene (HFO-1132) which has the above properties and withwhich excellent cycle performance will be obtained. Patent Documents 1and 2 also disclose an attempt to obtain a working fluid comprisingHFO-1123 or HFO-1132 and various HFCs of HFOs in combination for thepurpose of increasing the flame retardancy, cycle performance, etc. ofthe working fluid.

However, such a HFO is a compound having an unsaturated bond in itsmolecule and is a compound having a very short life in the air, andaccordingly under conditions under which compression and heating arerepeatedly carried out in a heat cycle, it is inferior in the stabilityto a saturated hydrofluorocarbon or hydrochlorofluorocarbon such as aconventional HFC or HCFC, and lubricating properties may be decreased inthe heat cycle system.

Thus, a method for efficiently operating a heat cycle system employing aHFO as a working fluid, with maintained lubricity while excellent cycleperformance of the HFO is sufficiently made use of.

PRIOR ART DOCUMENTS Patent Documents

Patent Document 1: WO2012/157764

Patent Document 2: WO2012/157765

DISCLOSURE OF INVENTION Technical Problem

The present invention has been made under these circumstances, and itsobject is to provide a composition for a heat cycle system comprising aHFO, with stable lubricity of the HFO, while the low global warmingpotential and excellent cycle performance of the HFO are sufficientlymade use of, and a heat cycle system employing the composition, whichhas less influence over global warm ing and has high cycle performance,and in which the lubricity of the working fluid for heat cycle isimproved.

Solution to Problem

The present invention provides a working fluid for heat cycle, acomposition for a heat cycle system and a heat cycle system of thefollowing [1] to [15].

[1] A composition for a heat cycle system comprising a working fluid forheat cycle containing at least one unsaturated fluorinated hydrocarboncompound selected from a compound having at least one carbon-carbonunsaturated bond in its molecule represented by the following formula(I), and

a refrigerant oil having a breakdown voltage of at least 25 kV, having ahydroxy value of at most 0.1 mgKOH/g, and a minimum temperature on thehigh temperature side of the phase separation temperature from theworking fluid for heat cycle of at least 35° C. and a maximumtemperature on the low temperature side of at most −60° C.:C_(x)F_(y)R_(z)  (I)wherein R is H or Cl, x is an integer of from 2 to 6, y is an integer offrom 1 to 12, and z is an integer of from 0 to 11, provided that2x≥y+z≥2.[2] The composition for a heat cycle system according to [1], whereinthe compound of the formula (I) wherein x is 2 or 3 is contained.[3] The composition for a heat cycle system according to [2], wherein asthe unsaturated fluorinated hydrocarbon compound, at least one memberselected from the group consisting of trifluoroethylene,2,3,3,3-tetrafluoropropene, 1,2-difluoroethylene, 2-fluoropropene,1,1,2-trifluoropropene, (E)-1,2,3,3,3-pentafluoropropene,(Z)-1,2,3,3,3-pentafluoropropene, (E)-1,3,3,3-tetrafluoropropene,(Z)-1,3,3,3-tetrafluoropropene and 3,3,3-trifluoropropene is contained.[4] The composition for a heat cycle system according to any one of [1]to [3], wherein the working fluid for heat cycle further contains asaturated fluorinated hydrocarbon compound.[5] The composition for a heat cycle system according to [4], wherein asthe saturated fluorinated hydrocarbon compound, at least one memberselected from the group consisting of trifluoromethane, difluoromethane,difluoroethane, trifluoroethane, tetrafluoroethane, pentafluoroethane,trifluoroiodomethane, pentafluoropropane, hexafluoropropane,heptafluoropropane, pentafluorobutane and heptafluorocyclopentane iscontained.[6] The composition for a heat cycle system according to any one of [1]to [5], wherein as the unsaturated fluorinated hydrocarbon compound,trifluoroethylene is contained, and the content of trifluoroethylene isfrom 20 to 80 mass % per 100 mass % of the working fluid for heat cycle.[7] The composition for a heat cycle system according to any one of [4]to [6], wherein as the saturated fluorinated hydrocarbon compound,difluoromethane is contained, and the content of difluoromethane is from20 to 80 mass % per 100 mass % of the working fluid for heat cycle.[8] The composition for a heat cycle system according to [4] or [5],wherein trifluoroethylene and 2,3,3,3-tetrafluoropropene are containedas the unsaturated fluorinated hydrocarbon compound, and difluoromethaneis contained as the saturated fluorinated hydrocarbon compound,

the proportion of the total amount of trifluoroethylene,2,3,3,3-tetrafluoropropene and difluoromethane based on the entireamount of the working fluid for heat cycle is higher than 90 mass % andat most 100 mass %, and

based on the total amount of trifluoroethylene,2,3,3,3-tetrafluoropropene and difluoromethane, the proportion by themass of trifluoroethylene is at least 10 mass % and less than 70 mass %,the proportion by the mass of 2,3,3,3-tetrafluoropropene is higher than0 mass % and at most 50 mass %, and the proportion by the mass ofdifluoromethane is higher than 30 mass % and at most 75 mass %.

[9] The composition for a heat cycle system according to [4] or [5],wherein trifluoroethylene and 2,3,3,3-tetrafluoropropene are containedas the unsaturated fluorinated hydrocarbon compound, and difluoromethaneis contained as the saturated fluorinated hydrocarbon compound,

the proportion of the total amount of trifluoroethylene,2,3,3,3-tetrafluoropropene and difluoromethane based on the entireamount of the working fluid for heat cycle is higher than 90 mass % andat most 100 mass %,

based on the total amount of trifluoroethylene,2,3,3,3-tetrafluoropropene and difluoromethane, the proportion by themass of the total amount of trifluoroethylene and2,3,3,3-tetrafluoropropene is at least 70 mass %, the proportion by themass of trifluoroethylene is at least 30 mass % and at most 80 mass %,the proportion by the mass of 2,3,3,3-tetrafluoropropene is higher than0 mass % and at most 40 mass %, and the proportion by the mass ofdifluoromethane is higher than 0 mass % and at most 30 mass %, and

the ratio of trifluoroethylene to 2,3,3,3-tetrafluoropropene is at most95/5.

[10] The composition for a heat cycle system according to any one of [1]to [9], wherein the refrigerant oil is at least one member selected froma polyol ester refrigerant oil and a polyvinyl ether refrigerant oil.

[11] The composition for a heat cycle system according to any one of [1]to [10], wherein the refrigerant oil has a kinematic viscosity at 40° C.of from 5 to 200 mm²/s and a kinematic viscosity at 100° C. of from 1 to100 mm²/s.

[12] The composition for a heat cycle system according to any one of [1]to [11], wherein the refrigerant oil has an aniline point of at least−100° C. and at most 0° C.

[13] A heat cycle system, which employs the composition for a heat cyclesystem as defined in any one of [1] to [12].

[14] The heat cycle system according to [13], which is at least onemember selected from a refrigerating apparatus, an air-conditioningapparatus, a power generation system, a heat transport apparatus and asecondary cooling machine.

[15] The heat cycle system according to [14], wherein the heat cyclesystem has a compression mechanism having a contact portion to be incontact with the composition for a heat cycle system, and the contactportion is composed of at least one member selected from an engineeringplastic, an organic film and an inorganic film.

Advantageous Effects of Invention

According to the present invention, it is possible to provide acomposition for a heat cycle system comprising an unsaturatedfluorinated hydrocarbon compound, with more stable lubricity of aworking fluid for heat cycle containing the unsaturated fluorinatedhydrocarbon compound, while the low global warming potential andexcellent cycle performance of the unsaturated fluorinated hydrocarboncompound are sufficiently made use of.

The heat cycle system of the present invention is a heat cycle systemwhich has less influence over global warming and has high cycleperformance, and in which the lubricating properties of the workingfluid for heat cycle are improved.

BRIEF DESCRIPTION OF DRAWINGS

FIG. 1 is a schematic construction view illustrating a refrigeratingcycle system as an example of a heat cycle system of the presentinvention.

FIG. 2 is a cycle diagram illustrating the state change of a workingfluid in a refrigerating cycle system in FIG. 1 on a pressure-enthalpychart.

DESCRIPTION OF EMBODIMENTS

Now, the present invention will be described in detail.

[Composition for Heat Cycle System]

The composition for a heat cycle system comprises a working fluid forheat cycle containing an unsaturated fluorinated hydrocarbon compound,and a refrigerant oil.

As a heat cycle system to which the composition of a heat cycle systemof the present invention is applied, a heat cycle system by a heatexchanger such as a condenser or an evaporator may be used without anyparticular restriction. The heat cycle system, for example, arefrigerating cycle system, has a mechanism in which a gaseous workingfluid is compressed by a compressor and cooled by a condenser to form ahigh pressure liquid, the pressure of the liquid is lowered by anexpansion valve, and the liquid is vaporized at low temperature by anevaporator so that heat is removed by the heat of vaporization.

When an unsaturated fluorinated hydrocarbon compound is used as aworking fluid for such a heat cycle system, depending upon thetemperature conditions and the pressure conditions, the unsaturatedfluorinated hydrocarbon compound may be destabilized and undergoself-decomposition, thus deteriorating the function of the working fluidfor heat cycle. In the composition for a heat cycle system of thepresent invention, by the coexistence of a refrigerant oil, lubricity ofthe unsaturated fluorinated hydrocarbon compound as a working fluid forheat cycle is improved, whereby efficient cycle performance can beexhibited.

Now, components in the composition for a heat cycle system of thepresent invention will be described.

<Working Fluid>

The composition for a heat cycle system of the present inventioncontains, as a working fluid, at least one unsaturated fluorinatedhydrocarbon compound selected from a compound having at least onecarbon-carbon unsaturated bond in its molecule represented by thefollowing formula (I):C_(x)F_(y)R_(z)  (I)wherein R is H or Cl, x is an integer of from 2 to 6, y is an integer offrom 1 to 12, and z is an integer of from 0 to 11, provided that2x≥y+z≥2.

The above formula (I) represents the types and the numbers of elementsin the molecule, and the formula (I) represents a fluorinated organiccompound in which the number x of carbon atoms C is from 2 to 6. A C₂₋₆fluorinated organic compound can have physical and chemical propertiesrequired for a working fluid, such as the boiling point, the freezingpoint and the latent heat of vaporization.

In the formula (I), the form of bond of x carbon atoms represented byC_(x) may be a carbon-carbon single bond, an unsaturated bond such as acarbon-carbon double bond, and the like, and the compound has at leastone carbon-carbon unsaturated bond. The unsaturated bond such as acarbon-carbon double bond is preferably a carbon-carbon double bond inview of stability, and its number is preferably 1.

Further, in the formula (I), R is either H or Cl, and R is preferably H,whereby such a compound is less likely to destroy the ozone layer.

Further, in the formula (I), the range of y+z is preferably at least 4.

[Unsaturated Fluorinated Hydrocarbon Compound]

In the present invention, the unsaturated fluorinated hydrocarboncompound used as the working fluid for a heat cycle system may be acompound represented by the formula (I) and may, for example, bepreferably a fluoride of a C₂₋₆ linear or branched chain olefin or aC₄₋₆ cyclic olefin.

Specifically, it may, for example, be ethylene having from 1 to 3fluorine atoms introduced, propene having from 1 to 5 fluorine atomsintroduced, a butene having from 1 to 7 fluorine atoms introduced, apentene having from 1 to 9 fluorine atoms introduced, a hexane havingfrom 1 to 11 fluorine atoms introduced, cyclobutene having from 1 to 5fluorine atoms introduced, cyclopenene having from 1 to 7 fluorine atomsintroduced, or cyclohexene having from 1 to 9 fluorine atoms introduced.

Among such unsaturated fluorinated hydrocarbon compounds, preferred is aC₂₋₃ unsaturated fluorinated hydrocarbon compound, more preferred is afluoride of C₂ ethylene. Such a C₂₋₃ unsaturated fluorinated hydrocarboncompound may, for example, be trifluoroethylene (HFO-1123),2,3,3,3-tetrafluoropropene (HFO-1234yf), 1,2-difluoroethylene(HFO-1132), 2-fluoropropene (HFO-1261yf), 1,1,2-trifluoropropene(HFO-1243yc), (E)-1,2,3,3,3-pentafluoropropene (HFO-1225ye(E)),(Z)-1,2,3,3,3-pentafluoropropene (HFO-1225ye(Z)),(E)-1,3,3,3-tetrafluoropropene (HFO-1234ze(E)),(Z)-1,3,3,3-tetrafluoropropene (HFO-1234ze(Z)) or 3,3,3-trifluoropropene(HFO-1243zf).

In the present invention, the unsaturated fluorinated hydrocarboncompound may be used alone or in combination of two or more.

The working fluid of the present invention may contain an optionalcomponent described hereinafter as the case requires in addition to theunsaturated fluorinated hydrocarbon compound of the formula (I). Thecontent of the unsaturated fluorinated hydrocarbon compound of theformula (I) is preferably at least 10 mass %, more preferably from 20 to80 mass %, further preferably from 40 to 80 mass %, still morepreferably from 40 to 60 mass % per 100 mass % of the working fluid.

(HFO-1123)

Now, a working fluid containing HFO-1123 as an essential component willbe described as an example of the unsaturated fluorinated hydrocarboncompound of the formula (I). However, HFO-1123 may be replaced with theunsaturated fluorinated hydrocarbon compound of the formula (I) otherthan HFO-1123.

First, properties of HFO-1123 as a working fluid are shown in Table 1particularly in terms of relative comparison with R410A (apseudoazeotropic mixture of HFC-32 and HFC-125 in a mass ratio of 1:1).The cycle performance is represented by the coefficient of performanceand the refrigerating capacity obtained by the after-mentioned method.The coefficient of performance and the refrigerating capacity ofHFO-1123 are represented by relative values based on R410A (1.000)(hereinafter referred to as relative coefficient of performance andrelative refrigerating capacity). The global warming potential (GWP) isa value (100 years) in Intergovernmental Panel on Climate Change (IPCC),Fourth assessment report (2007), or a value measured in accordancetherewith. In this specification, GWP is such a value unless otherwisespecified. In a case where the working fluid is a mixture, thetemperature glide is an important factor in evaluation of the workingfluid and is preferably smaller, as described hereinafter.

TABLE 1 R410A HFO-1123 Relative coefficient of 1.000 0.921 performanceRelative refrigerating 1.000 1.146 capacity Temperature glide 0.2 0 [°C.] GWP 2088 0.3[Optional Component]

The working fluid used in the present invention may optionally contain acompound commonly used for a working fluid, in addition to HFO-1123,within a range not to impair the effects of the present invention. Suchan optional compound (optional component) may, for example, be a HFC, aHFO (a HFC having a carbon-carbon double bond) other than HFO-1123, oranother component which is vaporized and liquefied together withHFO-1123. The optional component is preferably a HFC or a HFO (a HFChaving a carbon-carbon double bond) other than HFO-1123.

The optional component is preferably a compound which can maintain GWPand the temperature glide within acceptable ranges while having aneffect to further improve the relative coefficient of performance andthe relative refrigerating capacity, when used for heat cycle incombination with HFO-1123. When the working fluid contains such acompound in combination with HFO-1123, more favorable cycle performancewill be obtained while a low GWP is maintained, and influence over thetemperature glide tends to be small.

(Temperature Glide)

In a case where the working fluid contains an optional component, it hasa considerable temperature glide except for a case where HFO-1123 andthe optional component form an azeotropic composition. The temperatureglide of the working fluid varies depending upon the type of theoptional component and the mixture ratio of HFO-1123 and the optionalcomponent.

In a case where a mixture is used as the working fluid, it is usuallypreferably an azeotropic mixture or a pseudoazeotropic mixture such asR410A. A non-azeotropic composition has a problem such that when it isput into a refrigerator or an air-conditioning apparatus from a pressurecontainer, it undergoes a composition change. Further, if a refrigerantleaks out from a refrigerator or an air-conditioning apparatus, therefrigerant composition in the refrigerator or the air-conditioningapparatus is very likely to change, and a recovery to an initialrefrigerant composition is hardly possible. Such problems can be avoidedwith an azeotropic or pseudoazeotropic mixture.

As an index to the applicability of a mixture as the working fluid, the“temperature glide” is commonly employed. The temperature glide isdefined as properties such that the initiation temperature and thecompletion temperature of evaporation in an evaporator or ofcondensation in a condenser, for example, as the heat exchanger, differfrom each other. The temperature glide of an azeotropic mixture is 0,and the temperature glide of a pseudoazeotropic mixture is extremelyclose to 0, for example, the temperature glide of R410A is 0.2.

If the temperature glide is large, for example, the inlet temperature ofan evaporator tends to be low, and frosting is likely to occur. Further,in a heat cycle system, the heat exchange efficiency is to be improvedby making the working fluid and the heat source fluid such as water orthe air flowing in heat exchangers flow in counter-current flow. Sincethe temperature difference of the heat source fluid is small in a stableoperation state, it is difficult to obtain a heat cycle system with agood energy efficiency with a non-azeotropic mixture fluid with a largetemperature glide. Accordingly, when a mixture is used as a workingfluid, a working fluid with an appropriate temperature glide is desired.

(HFC)

The HFC as the optional component is preferably selected from the aboveviewpoint. Here, a HFC is known to have a higher GWP as compared withHFO-1123. Accordingly, the HFC to be used in combination with HFO-1123is preferably selected properly particularly with a view to maintainingGWP within an acceptable range, in addition to improving the cycleperformance as the working fluid and maintaining the temperature glidewithin an appropriate range.

A HFC which has less influence over the ozone layer and which has lessinfluence over global warming, is specifically preferably a C₁₋₅ HFC.The HFC may be linear, branched or cyclic.

The HFC may, for example, be a fluorinated C₁₋₅ alkane, and may bepreferably trifluoromethane, difluoromethane (HFC-32), difluoroethane,trifluoroethane, tetrafluoroethane, pentafluoroethane (HFC-125),trifluoroiodomethane, pentafluoropropane, hexafluoropropane,heptafluoropropane, pentafluorobutane, heptafluorocyclopentane or thelike.

Particularly, in view of less influence over the ozone layer andexcellent refrigerating cycle performance, the HFC is preferably HFC-32,1,1-difluoroethane (HFC-152a), 1,1,1-trifluoroethane (HFC-143a),1,1,2,2-tetrafluoroethane (HFC-134), 1,1,1,2-tetrafluoroethane(HFC-134a) or 1,1,1,2,2-pentafluoroethane (HFC-125), more preferablyHFC-32, HFC-152a, HFC-134a or HFC-125.

The HFC may be used alone or in combination of two or more.

The content of the HFC in the working fluid (100 mass %) can beoptionally selected depending upon the properties required for theworking fluid. For example, in the case of a working fluid comprisingHFO-1123 and HFC-32, the coefficient of performance and therefrigerating capacity will improve with a HFC-32 content within a rangeof from 1 to 99 mass %. In the case of a working fluid comprisingHFO-1123 and HFC-134a, the coefficient of performance will improve witha HFC-134a content within a range of from 1 to 99 mass %.

Further, with respect to GWP of the preferred HFC, GWP of HFC-32 is 675,GWP of HFC-134a is 1,430, and GWP of HFC-125 is 3,500. With a view tokeeping GWP of the obtainable working fluid low, the HFC as the optionalcomponent is most preferably HFC-32.

Further, HFO-1123 and HFC-32 may form a pseudoazeotropic mixture closeto an azeotropic mixture within a composition range of from 99:1 to 1:99by the mass ratio, and the temperature glide of a mixture of them isclose to 0 substantially regardless of the composition range. In thisview also, as the HFC to be used in combination with HFO-1123, HFC-32 isadvantageous.

In a case where HFC-32 is used together with HFO-1123 for the workingfluid of the present invention, the content of HFC-32 is specificallypreferably at least 20 mass %, more preferably from 20 to 80 mass %,further preferably from 40 to 60 mass % per 100 mass % of the workingfluid.

(HFO Other than HFO-1123)

The HFO other than HFO-1123 is also preferably selected from the sameviewpoint as the above HFC. Here, GWP of the HFO even other thanHFO-1123 is an order of magnitude lower than the HFC. Accordingly, theHFO other than HFO-1123 used in combination with HFO-1123 is preferablyselected properly particularly with a view to improving the cycleperformance as the working fluid and maintaining the temperature glidewithin an appropriate range, rather than considering GWP.

The HFO other than HFO-1123 may, for example, be2,3,3,3-tetrafluoropropene (HFO-1234yf), 1,2-difluoroethylene(HFO-1132), 2-fluoropropene (HFO-1261yf), 1,1,2-trifluoropropene(HFO-1243yc), (E)-1,2,3,3,3-pentafluoropropene (HFO-1225ye(E)),(Z)-1,2,3,3,3-pentafluoropropene (HFO-1225ye(Z)),(E)-1,3,3,3-tetrafluoropropene (HFO-1234ze(E)),(Z)-1,3,3,3-tetrafluoropropene (HFO-1234ze(Z)) or 3,3,3-trifluoropropene(HFO-1243zf).

Particularly, the HFO other than HFO-1123 is, in view of a high criticaltemperature and excellent durability and coefficient of performance,preferably HFO-1234yf (GSP:4), HFO-1234ze(E) or HFO-1234ze(Z) (GWPs ofboth (E)-form and (Z)-form being 6), more preferably HFO-1234yf. The HFOother than HFO-1123 may be used alone or in combination of two or more.

The content of the HFO other than HFO-1123 in the working fluid (100mass %) may be optionally selected depending upon the propertiesrequired for the working fluid. For example, in the case of a workingfluid comprising HFO-1123 and HFO-1234yf or HFO-1234ze, the coefficientof performance will improve with a HFO-1234yf or HFO-1234ze contentwithin a range of from 1 to 99 mass %.

A preferred composition range in a case where the working fluid used inthe present invention contains HFO-1123 and HFO-1234yf will be describedbelow as the composition range (S).

In the formulae indicating the composition range (S), abbreviated namesof the respective compounds indicate the proportions (mass %) of therespective compounds based on the entire amount of HFO-1123, HFO-1234yfand other components (such as HFC-32).

<Composition Range (S)>

HFO-1123+HFO-1234yf≥70 mass %

95 mass %≥HFO-1123/(HFO-1123+HFO-1234yf)≥35 mass %

The working fluid in the composition range (S) has a very low GWP andhas a small temperature glide. Further, it has refrigerating cycleperformance sufficient as an alternative to conventional R410A also fromthe viewpoint of the coefficient of performance, the refrigeratingcapacity and the critical temperature.

In the working fluid in the composition range (S), based on the totalamount of HFO-1123 and HFO-1234yf, the proportion of HFO-1123 is morepreferably from 40 to 95 mass %, further preferably from 50 to 90 mass%, particularly preferably from 50 to 85 mass %, most preferably from 60to 85 mass %.

Further, the total content of HFO-1123 and HFO-1234yf in 100 mass % ofthe working fluid is more preferably from 80 to 100 mass %, furtherpreferably from 90 to 100 mass %, particularly preferably from 95 to 100mass %.

Further, the working fluid used in the present invention may be acombination of HFO-1123, a HFC and a HFO other than HFO-1123. In such acase, the working fluid preferably comprises HFO-1123, HFC-32 andHFO-1234yf, and the proportions of the respective compounds based on theentire amount of the working fluid are preferably within the followingranges.

10 mass %≤HFO-1123≤80 mass %

10 mass %≤HFC-32≤75 mass %

5 mass %≤HFO-1234yf≤60 mass %

Further, in a case where the working fluid used in the present inventioncontains HFO-1123, HFO-1234yf and HFC-32, a preferred composition range(P) is shown below.

In the following formulae indicating the composition range (P),abbreviated names of the respective compounds indicate the proportions(mass %) of the respective compounds based on the entire amount ofHFO-1123, HFO-1234yf and HFC-32. The same applies to the compositionranges (R), (L) and (M). Further, in the following composition range,the total content of HFO-1123, HFO-1234yf and HFC-32 specificallydescribed is preferably higher than 90 mass % and at most 100 mass %based on the entire amount of the working fluid for heat cycle.

<Composition Range (P)>

70 mass %≤HFO-1123+HFO-1234yf

30 mass %≤HFO-1123≤80 mass %

0 mass %≤HFO-1234yf≤40 mass %

0 mass %<HFC-32≤30 mass %

HFO-1123/HFO-1234yf≤95/5 mass %

The working fluid in the above composition is a working fluid havingrespective characteristics of HFO-1123, HFO-1234yf and HFC-32 in abalanced manner, and having defects of the respective componentssuppressed. That is, the working fluid is a working fluid which has avery low GWP, has a small temperature glide and has a certainperformance and efficiency when used for heat cycle, and thus with sucha working fluid, favorable cycle performance will be obtained. Here, thetotal amount of HFO-1123 and HFO-1234yf based on the total amount ofHFO-1123, HFO-1234yf and HFC-32 is preferably at least 70 mass %.

Further, as a more preferred composition of the working fluid used inthe present invention, a composition containing HFO-1123 in a proportionof from 30 to 70 mass %, HFO-1234yf in a proportion of from 4 to 40 mass% and HFC-32 in a proportion of from 0 to 30 mass % based on the totalamount of HFO-1123, HFO-1234yf and HFC-32, and having a content ofHFO-1123 being at most 70 mol % based on the entire amount of theworking fluid, may be mentioned. A working fluid in the above range is aworking fluid of which self-decomposition reaction of HFO-1123 issuppressed, and which has high durability, in addition to the aboveeffects increased. From the viewpoint of the relative coefficient ofperformance, the content of HFC-32 is preferably at least 5 mass %, morepreferably at least 8 mass %.

Further, another preferred composition in a case where the working fluidused in the present invention contains HFO-1123, HFO-1234yf and HFC-32will be shown, and when the content of HFO-1123 based on the entireamount of the working fluid is at most 70 mol %, a working fluid ofwhich self-decomposition reaction of HFO-1123 is suppressed and whichhas high durability can be obtained.

A more preferred composition range (R) will be described below.

<Composition Range (R)>

10 mass %≤HFO-1123<70 mass %

0 mass %<HFO-1234yf≤50 mass %

30 mass %<HFC-32≤75 mass %

The working fluid in the above composition is a working fluid havingrespective characteristics of HFO-1123, HFO-1234yf and HFC-32 in abalanced manner, and having defects of the respective componentssuppressed. That is, it is a working fluid which has a low GWP, whichhas durability secured, and which has a small temperature glide and hashigh performance and efficiency when used for heat cycle, and thus withsuch a working fluid, favorable cycle performance will be obtained.

A preferred range of the working fluid of the present invention in thecomposition range (R) will be described below.

20 mass %≤HFO-1123<70 mass %

0 mass %<HFO-1234yf≤40 mass %

30 mass %<HFC-32≤75 mass %

The working fluid in the above composition is a working fluid havingrespective characteristics of HFO-1123, HFO-1234yf and HFC-32 in abalanced manner, and having defects of the respective componentssuppressed. That is, it is a working fluid which has a low GWP, whichhas durability secured, and which has a smaller temperature glide andhas higher performance and efficiency when used for heat cycle, and thuswith such a working fluid, favorable cycle performance will be obtained.

A more preferred composition range (L) of the working fluid of thepresent invention in the above composition range (R) will be describedbelow. A composition range (M) is still more preferred.

<Composition Range (L)>

10 mass %≤HFO-1123<70 mass %

0 mass %<HFO-1234yf≤50 mass %

30 mass %<HFC-32≤44 mass %

<Composition Range (M)>

20 mass %≤HFO-1123<70 mass %

5 mass %<HFO-1234yf≤40 mass %

30 mass %<HFC-32≤44 mass %

The working fluid in the composition range (M) is a working fluid havingrespective characteristics of HFO-1123, HFO-1234yf and HFC-32 in abalanced manner, and having defects of the respective componentssuppressed. That is, such a working fluid is a working fluid of whichthe upper limit of GWP is suppressed to be so low as at most 300, whichhas durability secured, and which has a small temperature glide of lessthan 5.8 and has a relative coefficient of performance and a relativerefrigerating capacity close to 1, when used for heat cycle, and thuswith such a working fluid, favorable cycle performance will be obtained.

Within such a range, the upper limit of the temperature glide islowered, and the lower limit of the product of the relative coefficientof performance and the relative refrigerating capacity is increased. Inview of a high relative coefficient of performance, more preferably 8mass %≤HFO-1234yf. Further, in view of a high relative refrigeratingcapacity, more preferably HFO-1234yf≤35 mass %.

(Other Optional Component)

The working fluid to be used for the composition for a heat cycle systemof the present invention may contain, other than the above optionalcomponent, carbon dioxide, a hydrocarbon, a chlorofluoroolefin (CFO), ahydrochlorofluoroolefin (HCFO), or the like. Such another optionalcomponent is preferably a component which has less influence over theozone layer and which has less influence over global warming.

The hydrocarbon may, for example, be propane, propylene, cyclopropane,butane, isobutane, pentane or isopentane.

The hydrocarbon may be used alone or in combination of two or more.

In a case where the working fluid contains a hydrocarbon, its content isless than 10 mass %, preferably from 1 to 5 mass %, more preferably from3 to 5 mass % per 100 mass % of the working fluid. When the content ofthe hydrocarbon is at least the lower limit, the solubility of a mineralrefrigerant oil in the working fluid will be more favorable.

The CFO may, for example, be chlorofluoropropene orchlorofluoroethylene. With a view to suppressing flammability of theworking fluid without significantly decreasing the cycle performance ofthe working fluid, the CFO is preferably1,1-dichloro-2,3,3,3-tetrafluoropropene (CFO-1214ya),1,3-dichloro-1,2,3,3-tetrafluoropropene (CFO-1214yb) or1,2-dichloro-1,2-difluoroethylene (CFO-1112).

The CFO may be used alone or in combination of two or more.

In a case where the working fluid contains the CFO, its content is lessthan 10 mass %, preferably from 1 to 8 mass %, more preferably from 2 to5 mass % per 100 mass % of the working fluid. When the content of theCFO is at least the lower limit, the flammability of the working fluidtends to be suppressed. When the content of the CFO is at most the upperlimit, favorable cycle performance is likely to be obtained.

The HCFO may, for example, be hydrochlorofluoropropene orhydrochlorofluoroethylene. With a view to suppressing flammability ofthe working fluid without significantly decreasing the cycle performanceof the working fluid, the HCFO is preferably1-chloro-2,3,3,3-tetrafluoropropene (HCFO-1224yd) or1-chloro-1,2-difluoroethylene (HCFO-1122).

The HCFO may be used alone or in combination of two or more.

In a case where the working fluid contains the HCFO, the content of theHCFO per 100 mass % of the working fluid is less than 1 mass %,preferably from 1 to 8 mass %, more preferably from 2 to 5 mass %. Whenthe content of the HCFO is at least the lower limit, the flammability ofthe working fluid tends to be suppressed. When the content of the HCFOis at most the upper limit, favorable cycle performance is likely to beobtained.

In a case where the working fluid to be used for the composition for aheat cycle system of the present invention contains the above otheroptional component, the total content of such optional components in theworking fluid is less than 10 mass %, preferably at most 8 mass %, morepreferably at most 5 mass % per 100 mass % of the working fluid.

<Refrigerant Oil>

The composition for a heat cycle system of the present inventioncomprises, in addition to the above working fluid, a refrigerant oilwhich can improve lubricating properties of the working fluid.

The refrigerant oil in the present invention has a breakdown voltage ofat least 25 kV. By using a refrigerant oil having a breakdown voltage ofat least 25 kV, insulation is maintained even in a heat cycle system inwhich an electromagnet for driving and the refrigerant oil are broughtinto direct contact with each other, and the heat cycle system will bestably operated. The breakdown voltage is more preferably at least 30kV, further preferably at least 40 kV. The breakdown voltage of arefrigerant oil in this specification is a value in a catalogue, or itis evaluated whether it is 25 kV or 50 kV or above or below bysimplified confirmation in accordance with JIS C2101.

Further, the refrigerant oil has a hydroxy value of at most 0.1 mgKOH/g.By the refrigerant oil having a sufficiently low hydroxy value of atmost 0.1 mgKOH/g, it is possible to prevent formation of hydroxyradicals which may cause deterioration by polymerization ordecomposition of the refrigerant oil or the working fluid for heatcycle. Hydroxy radicals are estimated, in a system using a working fluidhaving a carbon-carbon double bond, to attack and decompose the doublebond, thus generating an acid. If an acid is generated, corrosion ordeterioration of members or the like constituting the heat cycle systemmay occur. Accordingly, in the present invention in which the hydroxyvalue is low as mentioned above, generation of an acid can besignificantly suppressed, and the heat cycle system can be stablyoperated. The hydroxy value is more preferably at most 0.05 mgKOH/g. Thehydroxy value in this specification is measured in accordance with JISK2501.

Further, the refrigerant oil has a minimum temperature on the hightemperature side of at least 35° C. and a maximum temperature on the lowtemperature side of at most −60° C., of the phase separation temperaturefrom the working fluid for heat cycle of the above formula (I) used incombination. That is, such means that the working fluid for heat cycleand the refrigerant oil are present as being compatible with each otherunder conditions of operation of the heat cycle system, and in such acase, the heat cycle system can be stably operated since the compositionfor a heat cycle system in a liquid state does not undergo phaseseparation and is uniform. The minimum temperature on the hightemperature side of the phase separation temperature is at least 35° C.,preferably at least 40° C. The maximum temperature on the lowtemperature side is at most −60° C., preferably at most −70° C. Here, amixture of the working fluid for heat cycle and the refrigerant oil usedto measure the phase separation temperature is usually a mixturecontaining from 10 to 50 mass % of the refrigerant oil, and ispreferably a mixture having a content of the refrigerant oil of from 10to 20 mass %. The phase separation temperature in this specification isa value measured in accordance with JIS K2211.

Further, the kinematic viscosity of the refrigerant oil at 40° C. ispreferably from 5 to 200 mm²/s, more preferably from 5 to 100 mm²/s inthat the lubricity and the closeability of a compressor are not lowered,the lubricating machine oil is satisfactorily compatible with theworking fluid under low temperature conditions, it is possible toprevent lubricity failure of a refrigerator or a compressor, and heatexchange in an evaporator can be sufficiently conducted. Further, thekinematic viscosity at 100° C. is preferably from 1 to 100 mm²/s, morepreferably from 2 to 30 mm²/s, with a view to maintaining the electricpower consumption and the abrasion resistance within proper ranges. Thekinematic viscosity in this specification is a value measured inaccordance with JIS K2283.

Further, the refrigerant oil has an aniline point of preferably at least−100° C. and at most 0° C. “The aniline point” is a value indicating thesolubility of a hydrocarbon-based solvent for example, and is a valuemeasured in accordance with JIS K2256 in such a manner that equalvolumes of a sample (the refrigerant oil) and aniline are mixed andcooled, and the temperature at which they are no more miscible with eachother and turbidity starts being observed is recorded as the anilinepoint. Such a value is a value of the refrigerant oil by itself in whichno working fluid for heat cycle is dissolved.

In a heat cycle system to which the composition for a heat cycle systemcomprising the working fluid for heat cycle represented by the formula(I) of the present invention, since the working fluid has acarbon-carbon double bond, as described hereinafter, usually, an acidresistant resin material or the like as described in [heat cycle system]is employed in some part instead of a member made of a metal such ascopper commonly used as a member constituting a heat cycle system.However, even with such a resin material, depending upon the type ofrefrigerant oil used, the resin material may have drawbacks in somecases due to e.g. shrinkage or swelling resulting from the refrigerantoil. Accordingly, by using the refrigerant oil having an aniline pointwithin the above predetermined range (at least −100° C. and at most 0°C.), deformation by swelling/shrinkage of the resin material can beprevented, and it is possible to prevent a slide member in a compressionmechanism, an insulating material of an electric motor, a sealing memberin the interior of a heat cycle system, and the like from malfunctioningor breaking down due to deterioration or damages.

The refrigerant oil used in the present invention may, for example, bespecifically an oxygen-containing synthetic oil (an ester refrigerantoil, an ether refrigerant oil or a polyglycol refrigerant oil).

Among them, from the viewpoint of the compatibility with the fluorinatedhydrocarbon compound as an essential working fluid component in thepresent invention, an ester refrigerant oil or an ether refrigerant oilis suitable. Further, the ester refrigerant oil is preferably a polyolester refrigerant oil, and the ether refrigerant oil is preferably apolyvinyl ether refrigerant oil.

Particularly in the case of an ester refrigerant oil or an etherrefrigerant oil, as atoms constituting the refrigerant oil, carbon atomsand oxygen atoms are representatively mentioned. If the proportion(carbon/oxygen molar ratio) of carbon atoms to oxygen atoms is too low,moisture absorbance tends to be high, and if the proportion is too high,the compatibility with the working fluid will be decreased. From such aviewpoint, the proportion of carbon atoms to oxygen atoms in therefrigerant oil is suitably from 2 to 7.5 by the molar ratio.

<Ester Refrigerant Oil>

As the ester refrigerant oil, in view of chemical stability, a dibasicacid ester refrigerant oil of a dibasic acid and a monohydric alcohol, apolyol ester refrigerant oil of a polyol and a fatty acid, a complexester refrigerant oil of a polyol, a polybasic acid and a monohydricalcohol (or a fatty acid), a polyol carbonate ester refrigerant oil orthe like may be mentioned as the base oil component.

(Dibasic Acid Ester Refrigerant Oil)

The dibasic acid ester refrigerant oil is preferably an ester of adibasic acid such as oxalic acid, malonic acid, succinic acid, glutaricacid, adipic acid, pimelic acid, suberic acid, azelaic acid, sebacicacid, phthalic acid, isophthalic acid or terephthalic acid, particularlya C₅₋₁₀ dibasic acid (such as glutaric acid, adipic acid, pimelic acid,suberic acid, azelaic acid or sebacic acid) with a C₁₋₁₅ monohydricalcohol which is linear or has a branched alkyl group (such as methanol,ethanol, propanol, butanol, pentanol, hexanol, heptanol, octanol,nonanol, decanol, undecanol, dodecanol, tridecanol, tetradecanol orpentadecanol). Such a dibasic acid ester refrigerant oil may, forexample, be specifically ditridecyl glutarate, di(2-ethylhexyl) adipate,diisodecyl adipate, ditridecyl adipate or di(3-ethylhexyl) sebacate.

(Polyol Ester Refrigerant Oil)

The polyol ester refrigerant oil is an ester synthesized from apolyhydric alcohol and a fatty acid (a carboxylic acid).

The polyhydric alcohol constituting the polyol ester refrigerant oil maybe a diol (such as ethylene glycol, 1,3-propanediol, propylene glycol,1,4-butanediol, 1,2-butanediol, 2-methyl-1,3-propanediol,1,5-pentanediol, neopentyl glycol, 1,6-hexanediol,2-ethyl-2-methyl-1,3-propanediol, 1,7-heptanediol,2-methyl-2-propyl-1,3-propanediol, 2,2-diethyl-1,3-propanediol,1,8-octanediol, 1,9-nonanediol, 1,10-decanediol, 1,11-undecanediol or1,12-dodecanediol), a polyol having from 3 to 20 hydroxy groups (such astrimethylolethane, trimethylolpropane, trimethylolbutane,di-(trimethylolpropane), tri-(trimethylolpropane), pentaerythritol,di-(pentaerythritol), tri-(pentaerythritol), glycerin, polyglycerin (adimer or trimer of glycerin), 1,3,5-pentanetriol, sorbitol, sorbitan, asorbitol/glycerin condensate, a polyhydric alcohol such as adonitol,arabitol, xylitol or mannitol, a saccharide such as xylose, arabinose,ribose, rhamnose, glucose, fructose, galactose, mannose, sorbose,cellobiose, maltose, isomaltose, trehalose, sucrose, raffinose,gentianose or melezitose, or a partially etherified product thereof),and the polyhydric alcohol constituting the ester may be used alone orin combination of two or more.

The number of carbon atoms in the fatty acid constituting the polyolester refrigerant oil is not particularly limited, but usually a C₁₋₂₄fatty acid is employed. A linear fatty acid or a branched fatty acid ispreferred. The linear fatty acid may, for example, be acetic acid,propionic acid, butanoic acid, pentanoic acid, hexanoic acid, heptanoicacid, octanoic acid, nonanoic acid, decanoic acid, undecanoic acid,dodecanoic acid, tridecanoic acid, tetradecanoic acid, pentadecanoicacid, hexadecanoic acid, heptadecanoic acid, octadecanoic acid,nonadecanoic acid, eicosanoic acid, oleic acid, linoleic acid orlinoleic acid, and the hydrocarbon group bonded to the carboxy group maybe a totally saturated hydrocarbon or may have an unsaturatedhydrocarbon. Further, the branched fatty acid may, for example, be2-methylpropanoic acid, 2-methylbutanoic acid, 3-methylbutanoic acid,2,2-dimethylpropanoic acid, 2-methylpentanoic acid, 3-methylpentanoicacid, 4-methylpentanoic acid, 2,2-dimethylbutanoic acid,2,3-dimethylbutanoic acid, 3,3-dimethylbutanoic acid, 2-methylhexanoicacid, 3-methylhexanoic acid, 4-methylhexanoic acid, 5-methylhexanoicacid, 2,2-dimethylpentanoic acid, 2,3-dimethylpentanoic acid,2,4-dimethylpentanoic acid, 3,3-dimethylpentanoic acid,3,4-dimethylpentanoic acid, 4,4-dimethylpentanoic acid, 2-ethylpentanoicacid, 3-ethylpentanoic acid, 2,2,3-trimethylbutanoic acid,2,3,3-trimethylbutanoic acid, 2-ethyl-2-methylbutanoic acid,2-ethyl-3-methylbutanoic acid, 2-methylheptanoic acid, 3-methylheptanoicacid, 4-methylheptanoic acid, 5-methylheptanoic acid, 6-methylheptanoicacid, 2-ethylhexanoic acid, 3-ethylhexanoic acid, 4-ethylhexanoic acid,2,2-dimethylhexanoic acid, 2,3-dimethylhexanoic acid,2,4-dimethylhexanoic acid, 2,5-dimethylhexanoic acid,3,3-dimethylhexanoic acid, 3,4-dimethylhexanoic acid,3,5-dimethylhexanoic acid, 4,4-dimethylhexanoic acid,4,5-dimethylhexanoic acid, 5,5-dimethylhexanoic acid, 2-propylpentanoicacid, 2-methyloctanoic acid, 3-methyloctanoic acid, 4-methyloctanoicacid, 5-methyloctanoic acid, 6-methyloctanoic acid, 7-methyloctanoicacid, 2,2-dimethylheptanoic acid, 2,3-dimethylheptanoic acid,2,4-dimethylheptanoic acid, 2,5-dimethylheptanoic acid,2,6-dimethylheptanoic acid, 3,3-dimethylheptanoic acid,3,4-dimethylheptanoic acid, 3,5-dimethylheptanoic acid,3,6-dimethylheptanoic acid, 4,4-dimethylheptanoic acid,4,5-dimethylheptanoic acid, 4,6-dimethylheptanoic acid,5,5-dimethylheptanoic acid, 5,6-dimethylheptanoic acid,6,6-dimethylheptanoic acid, 2-methyl-2-ethylhexanoic acid,2-methyl-3-ethylhexanoic acid, 2-methyl-4-ethylhexanoic acid,3-methyl-2-ethylhexanoic acid, 3-methyl-3-ethylhexanoic acid,3-methyl-4-ethylhexanoic acid, 4-methyl-2-ethylhexanoic acid,4-methyl-3-ethylhexanoic acid, 4-methyl-4-ethylhexanoic acid,5-methyl-2-ethylhexanoic acid, 5-methyl-3-ethylhexanoic acid,5-methyl-4-ethylhexanoic acid, 2-ethylheptanoic acid, 3-methyloctanoicacid, 3,5,5-trimethylhexanoic acid, 2-ethyl-2,3,3-trimethylbutyric acid,2,2,4,4-tetramethylpentanoic acid, 2,2,3,3-tetramethylpentanoic acid,2,2,3,4-tetramethylpentanoic acid or 2,2-diisopropylpropanoic acid. Theester may be an ester of one or more of such fatty acids.

The polyol constituting the ester may be used alone or as a mixture oftwo or more. Further, the fatty acid constituting the ester may be asingle component or may be two or more types. Further, the fatty acidmay be used alone or as a mixture of two or more. Further, the polyolester refrigerant oil may have a free hydroxy group.

Among them, a particularly preferred polyol ester refrigerant oil ischaracterized by containing an ester obtained by using the followingcompounds (a) to (c):

(a) a compound having at least two hydroxy groups or its derivative,hydroxy groups,

(b) a compound having at least two carboxy groups or its derivative, and

(c) a compound having one carboxy group or its derivative and/or acompound having one hydroxy group or its derivative,

and being used together with the working fluid of the above formula (I),and can satisfy the lubricity, the sealing property, the compatibilitywith the working fluid, thermal/chemical stability, electricalinsulating properties, etc. sufficiently in a balanced manner, and cansufficiently prevent lubricity failure of a compressor and a decrease inthe refrigerating efficiency.

The compound (a) constituting the ester is a compound having at leasttwo hydroxy groups or its derivative. The number of hydroxy groups ispreferably from 2 to 6 in that an appropriate viscosity is secured andin view of the compatibility with the working fluid of the above formula(I). Further, if only a compound having one hydroxy group or itsderivative is used as the alcohol component, the obtainable ester hardlyhas a sufficient viscosity, lubricity failure or a decrease of therefrigerating efficiency tends to occur, and thermal/chemical stabilityor low temperature flowability tends to be insufficient.

The compound (a) may, for example, be specifically a polyhydric alcohol,a polyhydric phenol, a polyhydric aminoalcohol or a condensate thereof,or a compound having hydroxy groups of such a compound esterified by acarboxylic acid such as acetic acid, and among them, a polyhydricalcohol, its condensate or its derivative is preferred, whereby thecompatibility with the working fluid, electrical insulating propertiesand thermal stability tend to be more improved.

The number of carbon atoms in such a polyhydric alcohol is notparticularly limited, and a C₂₋₁₂ polyhydric alcohol is preferably used.As such a polyhydric alcohol, a dihydric alcohol (diol) may, forexample, be specifically ethylene glycol, 1,3-propanediol, propyleneglycol, 1,4-butanediol, 1,2-butanediol, 2-methyl-1,3-propanediol,1,5-pentanediol, neopentyl glycol, 1,6-hexanediol,2-ethyl-2-methyl-1,3-propanediol, 1,7-heptanediol,2-methyl-2-propyl-1,3-propanediol, 2,2-diethyl-1,3-propanediol,1,8-octanediol, 1,9-nonanediol, 1,10-decanediol, 1,11-undecanediol or1,12-dodecanediol. Further, a trihydric or higher alcohol may, forexample, be specifically a polyhydric alcohol such as trimethylolethane,trimethylolpropane, trimethylolbutane, di-(trimethylolpropane),tri-(trimethylolpropane), pentaerythritol, di-(pentaerythritol),tri-(pentaerythritol), glycerin, polyglycerin (a dimer or trimer ofglycerin), 1,3,5-pentanetriol, sorbitol, sorbitan, a sorbitol/glycerincondensate, adonitol, arabitol, xylitol or mannitol, a saccharide suchas xylose, arabinose, ribose, rhamnose, glucose, fructose, galactose,mannose, sorbose or cellobiose, or a partially etherified productthereof. Among them, preferred is a hindered alcohol such as neopentylglycol, trimethylolethane, trimethylolpropane, trimethylolbutane,di-(trimethylolpropane), tri-(trimethylolpropane), pentaerythritol ordi-(pentaerythritol).

Further, for the ester, as described above, as the compound (a), acompound having hydroxy groups esterified by a carboxylic acid may beused. Such a derivative is preferably a compound having hydroxy groupsesterified by a lower carboxylic acid, and specifically, an acetate orpropionate of the compound exemplified as the above polyhydric alcoholis preferably used.

The compound (b) constituting the above ester is a compound having atleast two carboxy groups or its derivative. The number of carboxy groupsis preferably from 2 to 6. If only a compound having one carboxy groupor its derivative is used as the acid component, the obtainable esterhardly has a sufficient viscosity, lubricity failure or a decrease ofthe refrigerating efficiency tends to occur, and thermal/chemicalstability or low temperature flowability tends to be insufficient.

The compound (b) may, for example, be a bivalent to hexavalentcarboxylic acid, or a carboxylic acid derivative such as its acidanhydride, ester or acid halide.

The number of carbon atoms in such a bivalent to hexavalent carboxylicacid is not particularly limited, and a C₂₋₁₀ bivalent carboxylic acidis preferably used. Such a bivalent to hexavalent carboxylic acid may,for example, be specifically a saturated aliphatic dicarboxylic acidsuch as oxalic acid, malonic acid, succinic acid, glutaric acid, adipicacid, pimelic acid, suberic acid, azelaic acid, sebacic acid,methylmalonic acid, ethylmalonic acid, dimethylmalonic acid,methylsuccinic acid, 2,2-dimethylsuccinic acid, 2,3-dimethylsuccinicacid, 2-ethyl-2-methylsuccinic acid, 2-methylglutaric acid,3-methylglutaric acid or 3-methyladipic acid; an unsaturated aliphaticdicarboxylic acid such as maleic acid, fumaric acid, itaconic acid,citraconic acid or mesaconic acid; an alicyclic dicarboxylic acid suchas 1,2-cyclohexanedicarboxylic acid or 4-cyclohexene-1,2-dicarboxylicacid; or an aromatic polyvalent carboxylic acid such as phthalic acid,terephthalic acid, isophthalic acid, trimellitic acid or pyromelliticacid, and among them, a bivalent carboxylic acid is preferred, and asaturated aliphatic dicarboxylic acid is more preferred in view ofoxidation stability.

Further, for the ester, as described above, as the compound (b), aderivative of a compound having two carboxy groups may be used. Such aderivative may, for example, be an ester, an acid anhydride or an acidhalide, and among them, an ester of the above bivalent carboxylic acidand a lower alcohol (more preferably methanol or ethanol) is preferablyused.

The compound (c) constituting the above ester is a compound having onecarboxy group or its derivative and/or a compound having one hydroxygroup or its derivative. As such a compound (c), either one of acompound having one carboxy group or its derivative and a compoundhaving one hydroxy group or its derivative may be used alone, or amixture of both may be used. If only a compound having at least twocarboxy groups or its derivative is used as the acid component and onlya compound having at least two hydroxy groups or its derivative is usedas the alcohol component, the obtainable ester tends to haveinsufficient thermal/chemical stability.

The compound having one carboxy group or its derivative may, forexample, be specifically a monovalent fatty acid, or its acid anhydride,ester or acid halide. The number of carbon atoms in such a monovalentfatty acid is not particularly limited, and a C₁₋₂₄ fatty acid iscommonly used, however, the number of carbon atoms in the monovalentfatty acid is preferably at least 3, more preferably at least 4, furtherpreferably at least 5, particularly preferably at least 8. If the numberof carbon atoms in the monovalent fatty acid is less than 3, thelubricity which the obtainable ester intrinsically has tends to beinsufficient, and in addition, the compatibility of the obtainable esterwith the working fluid of the above formula (I) will be excessivelyhigh, whereby the ester will be diluted with the working fluid and theviscosity tends to be low, thus leading to a decrease in therefrigerating efficiency and lubricity failure due to a decrease in thesealing property.

Further, the number of carbon atoms in the monovalent fatty acid ispreferably at most 22, more preferably at most 20, further preferably atmost 18. If the number of carbon atoms in the monovalent fatty acidexceeds 22, the compatibility of the obtainable ester with the workingfluid tends to be insufficient, thus leading to lubricity failure of acompressor and a decrease in the refrigerating efficiency due to adecrease in the oil return property.

The monovalent fatty acid as the compound (c) may be either linear orbranched, however, a linear monovalent fatty acid is preferred in viewof lubricity, and a branched monovalent fatty acid is preferred in viewof thermal/hydrolysis stability. Further, the monovalent fatty acid maybe either a saturated fatty acid or an unsaturated fatty acid.

The monovalent fatty acid as the compound (c) may, for example, bespecifically a linear or branched fatty acid such as pentaoic acid,hexanoic acid, heptanoic acid, octanoic acid, nonanoic acid, decanoicacid, undecanoic acid, dodecanoic acid, tridecanoic acid, tetradecanoicacid, pentadecanoic acid, hexadecanoic acid, heptadecanoic acid,octadecanoic acid, nonadecanoic acid, eicosanoic acid or oleic acid, ora fatty acid having a quaternary a carbon atom (a neo acid), and amongthem, valeric acid (n-pentanoic acid), caproic acid (n-hexanoic acid),enanthic acid (n-heptanoic acid), caprylic acid (n-octanoic acid),pelargonic acid (n-nonanoic acid), capric acid (n-decanoic acid), lauricacid (n-dodecanoic acid), myristic acid (n-tetradecanoic acid), palmiticacid (n-hexadecanoic acid), stearic acid (n-octadecanoic acid), oleicacid (cis-9-octadecenoic acid), isopentanoic acid (3-methylbutanoicacid), 2-methylhexanoic acid, 2-ethylpentanoic acid, 2-ethylhexanoicacid or 3,5,5-trim ethylhexanoic acid is preferably used.

Further, the compound having one hydroxy group or its derivative may,for example, be specifically a monohydric alcohol, a monohydric phenol,a monohydric aminoalcohol, or a compound having the hydroxy groups ofsuch a compound esterified by a carboxylic acid such as acetic acid. Thenumber of carbon atoms in such a compound is not particularly limited,and with a view to further improving both the lubricity and thecompatibility with the working fluid of the obtainable ester, preferredis a C₁₋₂₄ compound, and among them, preferred is a C₃₋₁₈ linearmonohydric alcohol, C₃₋₁₈ branched monohydric alcohol or a C₅₋₁₀monohydric cycloalcohol.

The monohydric alcohol having carbon atoms within the above preferredrange may, for example, be specifically a linear or branched propanol(including n-propanol, 1-methylethanol and the like), linear or branchedbutanol (including n-butanol, 1-methylpropanol, 2-methylpropanol and thelike), linear or branched pentanol (including n-pentanol,1-methylbutanol, 2-methylbutanol, 3-methylbutanol and the like), linearor branched hexanol (including n-hexanol, 1-methylpentanol,2-methylpentanol, 3-methylpentanol and the like), linear or branchedheptanol (including n-heptanol, 1-methylhexanol, 2-methylhexanol,3-methylhexanol, 4-methylhexanol, 5-methylhexanol, 2,4-dimethylpentanoland the like), linear or branched octanol (including n-octanol,2-ethylhexanol, 1-methylheptanol, 2-methylheptanol and the like), linearor branched nonanol (including n-nonanol, 1-methyloctanol,3,5,5-trimethylhexanol, 1-(2′-methylpropyl)-3-methylbutanol and thelike), linear or branched decanol (including n-decanol, isodecanol andthe like), linear or branched undecanol (including n-undecanol,isoundecanol and the like), linear or branched dodecanol (includingn-dodecanol, isododecanol, and the like), linear or branched tridecanol(including n-tridecanol, isotridecanol and the like), linear or branchedtetradecanol (including n-tetradecanol, isotetradecanol and the like),linear or branched pentadecanol (including n-pentadecanol,isopentadecanol and the like), linear or branched hexadecanol (includingn-hexadecanol, isohexadecanol and the like), linear or branchedheptadecanol (including n-heptadecanol, isoheptadecanol and the like),linear or branched octadecanol (including n-octadecanol, isooctadecanoland the like), cyclohexanol, methylcyclohexanol or dimethylcyclohexanol.

Further, as the compound (c), a derivative having the hydroxy groupesterified by a carboxylic acid may be used. Such a derivative ispreferably an acetate, propionate or the like of the compoundexemplified as the monohydric alcohol.

As the ester, particularly preferred is an ester obtained by using thefollowing compounds (a′), (b′) and (c′):

(a′) at least one member selected from the group consisting of ethyleneglycol, propylene glycol, butylene glycol, glycerin, neopentyl glycol,diethylene glycol, dipropylene glycol, dibutylene glycol and dibutyleneglycol,

(b′) at least one member selected from the group consisting of oxalicacid, malonic acid, succinic acid, glutaric acid, adipic acid, pymellicacid, suberic acid, azelaic acid and sebacic acid; and

(c′) at least one member selected from the group consisting of valericacid, caproic acid, enanthic acid, caprylic acid, pelargonic acid,capric acid, lauric acid, myristic acid, palmitic acid, stearic acid,oleic acid, isopentanoic acid, 2-methylhexanoic acid, 2-ethylpentanoicacid, 2-ethylhexanoic acid, 3,5,5-trimethylhexanoic acid, n-butanol,n-pentanol, n-hexanol, n-heptanol, n-octanol, n-nonanol, n-decanol,n-undecanol, n-dodecanol, n-tridecanol, n-tetradecanol, n-pentadecanol,n-hexadecanol, n-heptadecanol, n-octadecanol, isobutanol, isopentanol,isohexanol, isoheptanol, 2-ethylhexanol, 3,5,5-trimethylhexanol,isodecanol, isododecanol, isotetradecanol and isohexadecanol. When anester obtained by using the above compounds (a′) to (c′) is incorporatedin the refrigerant oil, the lubricity, the sealing property, thecompatibility with the working fluid, the thermal/chemical stability,the electrical insulating properties, etc. tend to be satisfied in abalanced manner.

The composition ratio of the above compounds (a) to (c) is notparticularly limited, however, the proportions of the compounds (a) to(c) are preferably within the following ranges, respectively, based onthe total amount of the compounds (a) to (c), whereby the lubricity, thesealing property, the compatibility with the working fluid, thethermal/chemical stability, the electrical insulating properties, etc.tend to be satisfied in a better balanced manner.

Compound (a): from 3 to 55 mol %, preferably from 5 to 50 mol %, morepreferably from 10 to 45 mol %.

Compound (b): from 3 to 55 mol %, preferably from 5 to 50 mol %, morepreferably from 10 to 45 mol %.

Compound (c): from 3 to 90 mol %, preferably from 5 to 80 mol %, morepreferably from 10 to 70 mol %.

The above-described ester is prepared by esterifying the above compounds(a) to (c) in accordance with a conventional method, preferably in anatmosphere of an inert gas such as nitrogen, in the presence of anesterifying catalyst or without a catalyst, with heating.

Further, in a case where an acetate, propionate or the like of analcohol is used as the compound (a) or (c) or in a case where a loweralcohol ester or the like of a carboxylic acid is used as the compound(b) or (c), the ester may be obtained by a transesterification reaction.

The esterifying catalyst used in the above esterification reaction, may,for example, be specifically a Lewis acid such as an aluminumderivative, a tin derivative or a titanium derivative; an alkali metalsalt such as a sodium alkoxide or a potassium alkoxide; or a sulfonicacid such as p-toluenesulfonic acid, methanesulfonic acid or sulfuricacid, and among them, a Lewis acid such as an aluminum derivative, a tinderivative or a titanium derivative is preferred, whereby the obtainableester has higher thermal/hydrolysis stability, and a tin derivative isparticularly preferred in view of the reaction efficiency. The amount ofthe esterifying catalyst is, for example, at a level of from 0.1 to 1mass % based on the total amount of the compounds (a) to (c) as the rawmaterials.

The reaction temperature in the above esterification reaction may, forexample, be from 150 to 230° C., and usually the reaction completes infrom 3 to 30 hours.

Further, after completion of the esterification reaction, the rawmaterials in excess may be distilled off under reduced pressure or undernormal pressure, and then a conventional purification method such asliquid-liquid extraction, vacuum distillation or adsorption purificationtreatment such as activated carbon treatment may be carried out topurify the ester.

Here, the esterification reaction using the specific compounds (a) to(c) has been described, however, even in other cases, the obtainablereaction product may be a mixture. Further, in a case where the ester isa mixture of at least two compounds, in view of the balance between thecompatibility with the working fluid and various performances, and theproduction easiness, the content of an ester having the compound (a) andthe compound (b) directly bonded is preferably from 10 to 100 mass %,more preferably from 20 to 100 mass %, further preferably from 25 to 100mass % based on the entire amount of the mixture.

(Complex Ester Refrigerant Oil)

The complex ester refrigerant oil is an ester of a fatty acid and adibasic acid, and a monohydric alcohol and a polyol. The fatty acid, thedibasic acid, the monohydric alcohol and the polyol may be the same asdescribed above.

The fatty acid may be a fatty acid exemplified for the above polyolester.

The dibasic acid may, for example, be oxalic acid, malonic acid,succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid,azelaic acid, sebacic acid, phthalic acid, isophthalic acid orterephthalic acid.

The polyol may be a polyol exemplified as the polyhydric alcohol for theabove polyol ester. The complex ester is an ester of such a fatty acid,a dibasic acid and a polyol, and each compound may consist of a singlecomponent or several components.

(Polyol Carbonate Refrigerant Oil)

The polyol carbonate refrigerant oil is an ester of carbonic acid and apolyol.

The polyol may, for example, be a polyglycol (such as polyalkyleneglycol, its ether compound or a modified compound thereof) obtained byhomopolymerizing or copolymerizing a diol (as described above), a polyol(as described above), or one having a polyglycol added to a polyol.

The polyalkylene glycol may, for example, be one obtained bypolymerizing a C₂₋₄ alkylene oxide (such as ethylene oxide or propyleneoxide) using water or an alkali hydroxide as an initiator. Further, itmay be one having a hydroxy group of a polyalkylene glycol etherified.One molecule of the polyalkylene glycol may contain single oxyalkyleneunits or two or more types of oxyalkylene units. It is preferred that atleast oxypropylene units are contained in one molecule. Further, thepolyol carbonate refrigerant oil may be a ring-opening polymer of acyclic alkylene carbonate.

<Ether Refrigerant Oil>

The ether refrigerant oil may, for example, be a polyvinyl etherrefrigerant oil or a polyalkylene glycol refrigerant oil.

(Polyvinyl Ether Refrigerant Oil)

The polyvinyl ether refrigerant oil may be one obtained by polymerizinga vinyl ether monomer, one obtained by copolymerizing a vinyl ethermonomer and a hydrocarbon monomer having an olefinic double bond, or acopolymer of a polyvinyl ether and an alkylene glycol or a polyalkyleneglycol or a monoether thereof.

Such a polyvinyl ether refrigerant oil is preferably a polyvinyl ethercompound having a structure represented by the following formula (1) andhaving a molecular weight of from 300 to 3,000:

wherein each of R¹, R² and R³ which are the same or different from eachother, is a hydrogen atom or a C₁₋₈ hydrocarbon group, R^(b) is a C₂₋₄bivalent hydrocarbon group, R^(a) is a hydrogen atom, a C₁₋₂₀ aliphaticor alicyclic hydrocarbon group, an aromatic group which may have a C₁₋₂₀substituent, a C₂₋₂₀ acyl group or a C₂₋₅₀ oxygen-containing hydrocarbongroup, R⁴ is a C₁₋₁₀ hydrocarbon group, and in a case where there are aplurality of each of R^(a), R^(b) and R⁴, they may be the same ordifferent, an average of m is from 1 to 50, o is a number of from 1 to50, and p is a number of from 2 to 25, and in a case where there are aplurality of o and p, the units may be either block or random,respectively.

The C₁₋₈ hydrocarbon group as each of R¹ to R³ may, for example, be analkyl group such as a methyl group, an ethyl group, a n-propyl group, anisopropyl group, a n-butyl group, an isobutyl group, a sec-butyl group,a tert-butyl group, various forms of a pentyl group, various forms of ahexyl group, various forms of a heptyl group or various forms of anoctyl group, a cycloalkyl group such as a cyclopentyl group, acyclohexyl group, various forms of a methylcyclohexyl group, variousforms of an ethylcyclohexyl group or various forms of adimethylcyclohexyl group, an aryl group such as a phenyl group, variousforms of a methylphenyl group, various forms of an ethylphenyl group orvarious forms of a dimethylphenyl group, or an arylalkyl group such as abenzyl group, various forms of a phenylethyl group or various forms of amethylbenzyl group. Each of R¹, R² and R³ is particularly preferably ahydrogen atom.

The C₂₋₄ bivalent hydrocarbon group represented by R^(b) is specificallya bivalent alkylene such as a methylene group, an ethylene group, apropylene group, a trim ethylene group or various forms of a butylenegroup.

m in the formula (1) represents the number of repetition of R^(b) O, andits average is within a range of from 1 to 50, preferably from 2 to 20,more preferably from 2 to 10, particularly preferably from 2 to 5. In acase where there are a plurality of R^(b) O, the plurality of R^(b) Omay be the same or different.

Further, o is a number of from 1 to 50, preferably from 1 to 10, morepreferably from 1 to 2, particularly preferably 1, and p is a number offrom 2 to 25, preferably from 5 to 15, and in a case where there are aplurality of each of o and p, the units may be block or random,respectively.

The C₁₋₂₀ aliphatic or alicyclic hydrocarbon group as R^(a) may bepreferably a C₁₋₁₀ alkyl group or a C₅₋₁₀ cycloalkyl group,specifically, a methyl group, an ethyl group, a n-propyl group, anisopropyl group, a n-butyl group, an isobutyl group, a sec-butyl group,a tert-butyl group, various forms of a pentyl group, various forms of ahexyl group, various forms of a heptyl group, various forms of an octylgroup, various forms of a nonyl group, various forms of a decyl group, acyclopentyl group, a cyclohexyl group, various forms of amethylcyclohexyl group, various forms of an ethylcyclohexyl group,various forms of a propylcyclohexyl group or various forms of a dimethylcyclohexyl group.

The aromatic group which may have a C₁₋₂₀ substituent as R^(a) may, forexample, be specifically an aryl group such as a phenyl group, variousforms of a tolyl group, various forms of an ethylphenyl group, variousforms of a xylyl group, various forms of a trimethylphenyl group,various forms of a butylphenyl group or various forms of a naphthylgroup, or an arylalkyl group such as a benzyl group, various forms of aphenylethyl group, various forms of a methylbenzyl group, various formsof a phenylpropyl group or various forms of a phenylbutyl group.

Further, the C₂₋₂₀ acyl group as R^(a) may, for example, be an acetylgroup, a propionyl group, a butyryl group, an isobutyryl group, avaleryl group, an isovaleryl group, a pivaloyl group, a benzoyl group ora toluoyl group.

The C₂₋₅₀ oxygen-containing hydrocarbon group as R^(a) may, for example,be specifically preferably a methoxymethyl group, a methoxyethyl group,a methoxypropyl group, a 1,1-bismethoxypropyl group, a1,2-bismethoxypropyl group, an ethoxypropyl group, a(2-methoxyethoxy)propyl group or a (1-methyl-2-methoxy)propyl group.

In the formula (1), the C₁₋₁₀ hydrocarbon group represented by R⁴ may,for example, be an alkyl group such as a methyl group, an ethyl group, an-propyl group, an isopropyl group, a n-butyl group, an isobutyl group,various forms of a pentyl group, various forms of a hexyl group, variousforms of a heptyl group, various forms of an octyl group, various formsof a nonyl group or various forms of decyl, a cycloalkyl group such as acyclopentyl group, a cyclohexyl group, various forms of amethylcyclohexyl group, various forms of an ethylcyclohexyl group,various forms of a propylcyclohexyl group or various forms of adimethylcyclohexyl group, an aryl group such as a phenyl group, variousforms of a methylphenyl group, various forms of an ethylphenyl group,various forms of a dimethylphenyl group, various forms of a propylphenylgroup, various forms of a trimethylphenyl group, various forms of abutylphenyl group or various forms of a naphthyl group, or an arylalkylgroup such as a benzyl group, various forms of a phenylethyl group,various forms of a methylbenzyl group, various forms of a phenylpropylgroup or various forms of a phenylbutyl group.

R¹ to R³, R^(a), R^(b), m and R¹ to R⁴ may be respectively the same ordiffered from each other with respect to the respective structuralunits.

The polyvinyl ether compound may be obtained, for example, bycopolymerizing a vinyl ether compound represented by the followingformula (2) and a vinyl ether compound represented by the followingformula (3):

In the above formulae, R^(a), R^(b), m and R¹ to R⁴ are as definedabove.

The vinyl ether compound represented by the formula (2) may, forexample, be an alkylene glycol monovinyl ether, a polyoxyalkylene glycolmonovinyl ether, an alkylene glycol alkyl vinyl ether or apolyoxyalkylene glycol alkyl vinyl ether. Specifically, it may, forexample, be ethylene glycol monovinyl ether, ethylene glycol methylvinyl ether, diethylene glycol monovinyl ether, diethylene glycol methylvinyl ether, triethylene glycol monovinyl ether, triethylene glycolmethyl vinyl ether, propylene glycol monovinyl ether, propylene glycolmethyl vinyl ether, dipropylene glycol monovinyl ether, dipropyleneglycol methyl vinyl ether, tripropylene glycol monovinyl ether ortripropylene glycol methyl vinyl ether.

Further, the vinyl ether compound represented by the formula (3) may,for example, be a vinyl ether such as vinyl methyl ether, vinyl ethylether, vinyl n-propyl ether, vinyl isopropyl ether, vinyl n-butyl ether,vinyl isobutyl ether, vinyl sec-butyl ether, vinyl tert-butyl ether,vinyl n-pentyl ether or vinyl n-hexyl ether; a propene such as1-methoxypropene, 1-ethoxypropene, 1-n-propoxypropene,1-isopropoxypropene, 1-n-butoxypropene, 1-isobutoxypropene,1-sec-butoxypropene, 1-tert-butoxypropene, 2-methoxypropene,2-ethoxypropene, 2-n-propoxypropene, 2-isopropoxypropene,2-n-butoxypropene, 2-isobutoxypropene, 2-sec-butoxypropene or2-tert-butoxypropene; or a butene such as 1-methoxy-1-butene,1-ethoxy-1-butene, 1-n-propoxy-1-butene, 1-isopropoxy-1-butene,1-n-butoxy-1-butene, 1-isobutoxy-1-butene, 1-sec-butoxy-1-butene,1-tert-butoxy-1-butene, 2-methoxy-1-butene, 2-ethoxy-1-butene,2-n-propoxy-1-butene, 2-isopropoxy-1-butene, 2-n-butoxy-1-butene,2-isobutoxy-1-butene, 2-sec-butoxy-1-butene, 2-tert-butoxy-1-butene,2-methoxy-2-butene, 2-ethoxy-2-butene, 2-n-propoxy-2-butene,2-isopropoxy-2-butene, 2-n-butoxy-2-butene, 2-isobutoxy-2-butene,2-sec-butoxy-2-butene or 2-tert-butoxy-2-butene. Such a vinyl ethermonomer may be prepared by a known method.

The above vinyl ether compound may be produced by e.g. radicalpolymerization, cationic polymerization or radiation polymerization of acorresponding vinyl ether compound and a hydrocarbon monomer having anolefinic double bond used if desired. For example, a vinyl ether monomeris polymerized by the following method to obtain a polymer having adesired viscosity. To initiate polymerization, a combination of aBronsted acid, a Lewis acid or an organic metal compound, with water, analcohol, a phenol, an acetal or an adduct of a vinyl ether and acarboxylic acid, may be used. The Bronsted acid may, for example, behydrofluoric acid, hydrochloric acid, hydrobromic acid, hydroiodic acid,nitric acid, sulfuric acid, trichloroacetic acid or trifluoroaceticacid. The Lewis acid may, for example, be boron trifluoride, aluminumtrichloride, aluminum tribromide, tin tetrachloride, zinc dichloride orferric chloride, and among such Lewis acids, boron trifluoride isparticularly suitable. Further, the organic metal compound may, forexample, be diethyl aluminum chloride, ethyl aluminum chloride ordiethyl zinc.

As the water, alcohol, phenol, acetal or adduct of a vinyl ether and acarboxylic acid to be combined therewith, an optional one may beselected. The alcohol may, for example, be a C₁₋₂₀ saturated aliphaticalcohol such as methanol, ethanol, propanol, isopropanol, butanol,isobutanol, sec-butanol, tert-butanol, various forms of pentanol,various forms of hexanol, various forms of heptanol or various forms ofoctanol, a C₃₋₁₀ unsaturated aliphatic alcohol such as allyl alcohol, ora monoether of an alkylene glycol such as ethylene glycol monomethylether, diethylene glycol monomethyl ether, triethylene glycol monomethylether, propylene glycol monomethyl ether, dipropylene glycol monomethylether or tripropylene glycol monomethyl ether. In a case where an adductof a vinyl ether and a carboxylic acid is used, the carboxylic acid may,for example, be acetic acid, propionic acid, n-butyric acid, isobutyricacid, n-valeric acid, isovaleric acid, 2-methylbutyric acid, pivalicacid, n-caproic acid, 2,2-dimethylbutyric acid, 2-methylvaleric acid,3-methylvaleric acid, 4-methylvaleric acid, enanthic acid,2-methylcaproic acid, caprylic acid, 2-ethylcaproic acid,2-n-propylvaleric acid, n-nonanoic acid, 3,5,5-trimethylcaproic acid,caprylic acid or undecanoic acid.

Further, in a case where an adduct of a vinyl ether and a carboxylicacid is used, the vinyl ether may be the same as or different from oneused for polymerization. The adduct of a vinyl ether and a carboxylicacid may be obtained by mixing them to allow them to react at atemperature of from about 0 to about 100° C., and the adduct may beseparated e.g. by distillation and used for reaction, or it may be usedfor the reaction as it is without separation.

The polymerization initiation terminal of the resulting polymer hashydrogen bonded in a case where water, an alcohol or a phenol is used,and in a case where on acetal is used, it has hydrogen or one of alkoxygroups left from the acetal used. Further, in a case where an adduct ofa vinyl ether and a carboxylic acid is used, it has an alkylcarbonyloxygroup derived from the carboxylic acid moiety left from the adduct of avinyl ether and a carboxylic acid.

Further, the termination terminal is an acetal, an olefin or an aldehydein a case where water, an alcohol, a phenol or an acetal is used.Further, in the case of an adduct of a vinyl ether and a carboxylicacid, it is a carboxylate of a hemiacetal. The terminal of the polymerthus obtained may be converted into a desired group by a known method.Such a desired group may, for example, be a residue of e.g. a saturatedhydrocarbon, an ether, an alcohol, a ketone, a nitrile or an amide, andis preferably a residue of a saturated hydrocarbon, an ether or analcohol.

The polyvinyl ether compound contained in the refrigerant oil used inthe present invention has a carbon/oxygen molar ratio of at least 4. Ifthe molar ratio exceeds 4, the compatibility with the working fluid ofthe formula (I) will be decreased. With respect to adjustment of themolar ratio, a polymer having the molar ratio being within the aboverange can be produced by adjusting the carbon/oxygen molar ratio of theraw material monomer. That is, a polymer having a high carbon/oxygenmolar ratio will be obtained when the proportion of a monomer having acarbon/oxygen molar ratio is high, and a polymer having a lowcarbon/oxygen molar ratio will be obtained when the proportion of themonomer having a low carbon/oxygen molar ratio is high. Further, thecarbon/oxygen molar ratio may be adjusted also by a combination of themonomers with water, an alcohol, a phenol, an acetal or an adduct of avinyl ether and a carboxylic acid used as the initiator, as describedfor the method of polymerizing the vinyl ether monomer. A polymer havinga carbon/oxygen molar ratio higher than the raw material monomer will beobtained by using as the initiator an alcohol, a phenol or the likehaving a carbon/oxygen molar ratio higher than the monomer to bepolymerized, and a polymer having a carbon/oxygen molar ratio lower thanthe raw material monomer will be obtained by using an alcohol having alow carbon/oxygen molar ratio such as methanol or methoxyethanol.

Further, in a case where a vinyl ether monomer and a hydrocarbon monomerhaving an olefinic double bond are copolymerized, a polymer having acarbon/oxygen molar ratio higher than the carbon/oxygen molar ratio ofthe vinyl ether monomer will be obtained, and the proportion may beadjusted by the proportion of the hydrocarbon monomer having an olefinicdouble bond used and its number of carbon atoms.

(Polyalkylene Glycol Refrigerant Oil)

The polyalkylene glycol refrigerant oil may, for example, be oneobtained by polymerizing a C₂₋₄ alkylene oxide (such as ethylene oxideor propylene oxide) using water or an alkali hydroxide as an initiator.Further, it may be one having a hydroxy group of a polyalkylene glycoletherified. One molecule of the polyalkylene glycol refrigerant oil maycontain single oxyalkylene units or two or more types of oxyalkyleneunits. It is preferred that at least oxypropylene units are contained inone molecule.

A specific polyoxyalkylene glycol refrigerant oil may, for example, be acompound represented by the following formula (4):R¹⁰¹—[(OR¹⁰²)_(k)—OR¹⁰³]_(l)  (4)wherein R¹⁰¹ is a hydrogen atom, a C₁₋₁₀ alkyl group, a C₂₋₁₀ acyl groupor a C₁₋₁₀ aliphatic hydrocarbon group having 2 to 6 binding sites, R¹⁰²is a C₂₋₄ alkylene group, R¹⁰³ is a hydrogen atom, a C₁₋₁₀ alkyl groupor a C₂₋₁₀ acyl group, l is an integer of from 1 to 6, and k is a numberwhich makes the average of k×l from 6 to 80.

In the above formula (4), the alkyl group as each of R¹⁰¹ and R¹⁰³ maybe linear, branched or cyclic. The alkyl group may, for example, bespecifically a methyl group, an ethyl group, a n-propyl group, anisopropyl group, various forms of a butyl group, various forms of apentyl group, various forms of a hexyl group, various forms of a heptylgroup, various forms of an octyl group, various forms of a nonyl group,various forms of a decyl group, a cyclopentyl group or a cyclohexylgroup. If the number of carbon atoms in the alkyl group exceeds 10, thecompatibility with the working fluid will be decreased, thus leading tophase separation. The number of carbon atoms in the alkyl group ispreferably from 1 to 6.

The alkyl group moiety in the acyl group as each of R¹⁰¹ and R¹⁰³ may belinear, branched or cyclic. As specific examples of the alkyl groupmoiety in the acyl group, various C₁₋₉ groups mentioned as the specificexamples of the alkyl group may be mentioned. If the number of carbonatoms in the acyl group exceeds 10, the compatibility with the workingfluid will be decreased, thus leading to phase separation. The number ofcarbon atoms in the acyl group is preferably from 2 to 6.

In a case where both R¹⁰¹ and R¹⁰³ are an alkyl group or an acyl group,R¹⁰¹ and R¹⁰³ may be the same or different from each other.

Further, in a case where l is at least 2, the plurality of R¹⁰³ in onemolecule may be the same or different from each other.

In a case where R¹⁰¹ is a C₁₋₁₀ aliphatic hydrocarbon group having from2 to 6 binding sites, the aliphatic hydrocarbon group may be chain-likeor cyclic. The aliphatic hydrocarbon group having two binding sites may,for example, be an ethylene group, a propylene group, a butylene group,a pentylene group, a hexylene group, a heptylene group, an octylenegroup, a nonylene group, a decylene group, a cyclopentylene group or acyclohexylene group. Further, an aliphatic hydrocarbon group having from3 to 6 binding sites may, for example, be trimethylolpropane, glycerin,pentaerythritol, sorbitol; 1,2,3-trihydroxycyclohexane; or a residuehaving a hydroxy group removed from a polyhydric alcohol such as1,3,5-trihydroxycyclohexane.

If the number of carbon atoms in the aliphatic hydrocarbon group exceeds10, the compatibility with the working fluid will be decreased, thusleading to a phase separation. The number of carbon atoms is preferablyform 2 to 6.

R¹⁰² in the above formula (4) is a C₂₋₄ alkylene group, and theoxyalkylene group as a repeating unit may be an oxyethylene group, anoxypropylene group or an oxybutylene group. One molecule of the compoundof the formula (4) may contain single type of oxyalkylene groups or twoor more types of oxyalkylene groups. It is preferred that at leastoxypropylene units are contained in one molecule, and it is particularlypreferred that at least 50 mol % of oxypropylene units are contained inoxyalkylene units.

In the above formula (4), l is an integer of from 1 to 6 and is defineddepending upon the number of the binding sites of R¹⁰¹. For example, ina case where R¹⁰¹ is an alkyl group or an acyl group, l is 1, and in acase where R¹⁰¹ is an aliphatic hydrocarbon group having 2, 3, 4, 5 or 6binding sites, l is 2, 3, 4, 5 or 6, respectively. Further, k is anumber which makes the average of k×l from 6 to 80, and if the averageof k×l is out of the above range, the objects of the present inventionwill not sufficiently be accomplished.

The structure of the polyalkylene glycol is suitably polypropyleneglycol dimethyl ether represented by the following formula (5) orpoly(oxyethylene oxypropylene) glycol dimethyl ether represented by thefollowing formula (6) in view of economical efficiency and theabove-described effects, and is more preferably polypropylene glycolmonobutyl ether represented by the following formula (7), furthersuitably polypropylene glycol monomethyl ether represented by thefollowing formula (8), poly(oxyethylene oxypropylene) glycol monomethylether represented by the following formula (9), poly(oxyethyleneoxypropylene) glycol monobutyl ether represented by the followingformula (10) or polypropylene glycol diacetate represented by thefollowing formula (11) in view of economical efficiency, etc.CH₃O—(C₃H₆O)_(h)—CH₃  (5)(wherein h is a number of from 6 to 80)CH₃O—(C₂H₄O)_(i)—(C₃H₆O)_(j)—CH₃  (6)(wherein each of i and j is a number of at least 1, provided that thesum of i and j is from 6 to 80)C₄H₉O—(C₃H₆O)_(h)—H  (7)(wherein h is a number of from 6 to 80)CH₃O—(C₃H₆O)_(h)—H  (8)(wherein h is a number of from 6 to 80)CH₃O—(C₂H₄O)_(i)—(C₃H₆O)_(j)—H  (9)(wherein each of i and j is a number of at least 1, provided that thesum of i and j is from 6 to 80)C₄H₉O—(C₂H₄O)_(i)—(C₃H₆O)_(j)—H  (10)(wherein each of i and j is a number of at least 1, provided that thesum of i and j is from 6 to 80)CH₃COO—(C₃H₆O)_(h)—COCH₃  (11)(wherein h is a number of from 6 to 80)

Such polyoxyalkylene glycols may be used alone or in combination of twoor more.

The above refrigerant oils may be used alone or in combination of two ormore.

Such a refrigerant oil is preferably used as a composition for a heatcycle system as mixed with the working fluid. On that occasion, theproportion of the refrigerant oil is preferably from 5 to 60 mass %,more preferably from 10 to 50 mass % based on the entire amount of thecomposition for a heat cycle system.

Further, the moisture content of the refrigerant oil is not particularlylimited, and is preferably at most 300 ppm, more preferably at most 200ppm, most preferably at most 100 ppm based on the entire amount of therefrigerant oil. Particularly in a case where it is used for a closedrefrigerator, a low moisture content is required from the viewpoint ofthe decomposition stability of the working fluid, and the influence ofthe refrigerant oil over the thermal/chemical stability and theelectrical insulating properties. In this specification, the moisturecontent was measured in accordance with JIS K2275.

The remaining air partial pressure of the refrigerant oil is notparticularly limited, and is preferably at most 10 kPa, more preferablyat most 5 kPa.

Further, the ash of the refrigerant oil used is not particularlylimited, and is preferably at most 100 ppm, more preferably at most 50ppm, so as to increase the thermal/chemical stability of the refrigerantoil and to prevent occurrence of sludge and the like. In thisspecification, the ash means a value of the ash measured in accordancewith JIS K2272.

<Other Optional Component>

The composition for a heat cycle system may contain a known optionalcomponent in addition within a range not to impair the effects of thepresent invention. Such an optional component may, for example, be anadditive which makes the refrigerant oil be stably contained in thecomposition for a heat cycle system, and such an additive may, forexample, be a copper deactivator, an extreme-pressure agent, an oilagent, an antioxidant, an acid scavenger, an antifoaming agent or apolymerization inhibitor. Each additive may be added as the caserequires, and the amount of each additive is set to be at least 0.01mass % and at most 5 mass % in 100 mass % of the composition for a heatcycle system. Here, the amount of the acid scavenger and the amount ofthe antioxidant are preferably within a range of at least 0.05 mass %and at most 5 mass %.

As the copper deactivator, benzotriazole, its derivative or the like maybe used. As the antifoaming agent, a silicon compound may be used. Asthe oil agent, a higher alcohol may be used.

Further, as the extreme-pressure agent, one containing a phosphoric acidester may be used. As the phosphoric acid ester, a phosphate, aphosphite, an acidic phosphate, an acidic phosphite or the like may beused. Further, as the extreme-pressure agent, one containing an aminesalt of a phosphate, a phosphite, an acidic phosphate or an acidicphosphite may be used.

The phosphate may, for example, be triaryl phosphate, trialkylphosphate, trialkyl aryl phosphate, triaryl alkyl phosphate ortrialkenyl phosphate. Further, the phosphate may, for example, bespecifically triphenyl phosphate, tricresyl phosphate, benzyl diphenylphosphate, ethyl diphenyl phosphate, tributyl phosphate, ethyl dibutylphosphate, cresyl diphenyl phosphate, dicresyl phenyl phosphate,ethylphenyl diphenyl phosphate, diethylphenyl phenyl phosphate,propylphenyl diphenyl phosphate, dipropylphenyl phenyl phosphate,triethylphenyl phosphate, tripropylphenyl phosphate, butylphenyldiphenyl phosphate, dibutylphenyl phenyl phosphate, tributylphenylphosphate, trihexyl phosphate, tri(2-ethylhexyl) phosphate, tridecylphosphate, trilauryl phosphate, trimyristyl phosphate, tripalmitylphosphate, tristearyl phosphate or trioleyl phosphate.

Further, the phosphite may, for example, be specifically triethylphosphite, tributyl phosphite, triphenyl phosphite, tricresyl phosphite,tri(nonylphenyl) phosphite, tri(2-ethylhexyl) phosphite, tridecylphosphite, trilauryl phosphite, triisooctyl phosphite, diphenyl isodecylphosphite, tristearyl phosphite or trioleyl phosphite.

Further, the acidic phosphate may, for example, be 2-ethylhexylacidphosphate, ethyl acid phosphate, butyl acid phosphate, oleyl acidphosphate, tetracosyl acid phosphate, isodecyl acid phosphate, laurylacid phosphate, tridecyl acid phosphate, stearyl acid phosphate orisostearyl acid phosphate.

Further, the acidic phosphite may, for example, be dibutyl hydrogenphosphite, dilauryl hydrogen phosphite, dioleyl hydrogen phosphite,distearyl hydrogen phosphite or diphenyl hydrogen phosphite. Among theabove phosphoric acid esters, oleyl acid phosphate or stearyl acidphosphate is suitable.

Further, among amines to be used for the amine salt of a phosphate, aphosphite, an acidic phosphate or an acidic phosphite, amono-substituted amine may, for example, be specifically butylamine,pentylamine, hexylamine, cyclohexylamine, octylamine, laurylamine,stearylamine, oleylamine or benzylamine. Further, a di-substituted aminemay, for example, be specifically dibutylamine, dipentylamine,dihexylamine, dicyclohexylamine, dioctylamine, dilaurylamine,distearylamine, dioleylamine, dibenzylamine, stearyl monoethanolamine,decyl monoethanolamine, hexyl monopropanolamine, benzylmonoethanolamine, phenyl monoethanolamine or tolyl monopropanol.Further, a tri-substituted amine may, for example, be specificallytributylamine, tripentylamine, trihexylamine, tricyclohexylamine,trioctylamine, trilaurylamine, tristearylamine, trioleylamine,tribenzylamine, dioleyl monoethanolamine, dilauryl monopropanolamine,dioctyl monoethanolamine, dihexyl monopropanolamine, dibutylmonopropanolamine, oleyl diethanolamine, stearyl dipropanolamine, lauryldiethanolamine, octyl dipropanolamine, butyl diethanolamine, benzyldiethanolamine, phenyl diethanolamine, tolyl dipropanolamine, xylyldiethanolamine, triethanolamine or tripropanolamine.

Further, an extreme-pressure agent other than the above may be added.For example, it is possible to use an organic sulfur-containing compoundtype extreme-pressure agent such as a monosulfide, a polysulfide, asulfoxide, a sulfone, a thiosulfinate, a sulfurised oil, athiocarbonate, a thiophene, a thiazole or a methanesulfonate, athiophosphate type extreme-pressure agent such as a thiophosphoric acidtriester, an ester type extreme-pressure agent such as a higher fattyacid, a hydroxyaryl fatty acid, a polyhydric alcohol ester or anacrylate, an organic chlorine type extreme-pressure agent such as achlorinated hydrocarbon or a chlorinated carboxylic acid derivative, anorganic fluorinated compound type extreme-pressure agent such as afluorinated aliphatic carboxylic acid, a fluorinated ethylene resin, afluorinated alkylpolysiloxane or fluorinated graphite, an alcohol typeextreme-pressure agent such as a higher alcohol, or a metal compoundtype extreme-pressure agent such as a naphthenate (such as leadnaphthenate) a fatty acid salt (such as fatty acid lead salt), athiophosphate (such as zinc dialkyldithiophosphate), a thiocarbamate, anorganic molybdenum compound, an organic tin compound, an organicgermanium compound or a borate ester.

Further, as the antioxidant, a phenol type antioxidant or an amine typeantioxidant may be used. The phenol type antioxidant may, for example,be 2,6-di-tert-butyl-4-methylphenol (DBPC),2,6-di-tert-butyl-4-ethylphenol,2,2′-methylenebis(4-methyl-6-tert-butylphenol),2,4-dimethyl-6-tert-butylphenol or 2,6-di-tert-butylphenol. Further, theamine type antioxidant may, for example, beN,N′-diisopropyl-p-phenylenediamine,N,N′-di-sec-butyl-p-phenylenediamine, N-phenyl-1-naphthylamine orN,N′-diphenyl-p-phenylenediamine. Further, for the antioxidant, an acidscavenger to scavenge oxygen may also be used.

As the acid scavenger, an epoxy compound such as phenyl glycidyl ether,an alkyl glycidyl ether, an alkylene glycol glycidyl ether, cyclohexeneoxide, an α-olefin oxide or epoxidized soybean oil may be used. Amongthem, from the viewpoint of the compatibility, preferred as an acidscavenger is phenyl glycidyl ether, an alkyl glycidyl ether, an alkyleneglycol glycidyl ether, cyclohexene oxide or an α-olefin oxide. The alkylgroup in the alkyl glycidyl ether and the alkylene group in the alkyleneglycol glycidyl ether may be branched. The number of carbon atoms insuch a compound is at least 3 and at most 30, preferably at least 4 andat most 24, further preferably at least 6 and at most 16. Further, thetotal number of carbon atoms in the α-olefin oxide is at least 4 and atmost 50, preferably at least 4 and at most 24, more preferably at least6 and at most 16. Such acid scavengers may be used alone or incombination of two or more.

Further, as the polymerization inhibitor, a polymerization inhibitorsuch as 4-methoxy-1-naphthol, hydroquinone, hydroquinone methyl ether,dimethyl-tert-butyl phenol, 2,6-di-tert-butyl-p-cresole or benzotriazolemay be used.

Further, to the composition for a heat cycle system according to thisembodiment, as the case requires, a load-carrying additive, an oxygenscavenger, a chlorine scavenger, a detergent-dispersant, a viscosityindex improver, an anticorrosive, a stabilizer, a corrosion inhibitor, apour-point depressant or the like may be added. The oxygen scavenger isan additive to scavenge oxygen. The amount of each additive is at least0.01 mass % and at most 5 mass %, preferably at least 0.05 mass % and atmost 2 mass % in 100 mass % of the composition for a heat cycle system.

Further, as an optional component to be blended in the composition for aheat cycle system, for example, a leak detecting substance may bementioned, and such a leak detecting substance optionally contained may,for example, be an ultraviolet fluorescent dye, an odor gas or an odormasking agent.

The ultraviolet fluorescent dye may be known ultraviolet fluorescentdyes which have been used for a heat cycle system together with aworking fluid comprising a halogenated hydrocarbon, such as dyes asdisclosed in e.g. U.S. Pat. No. 4,249,412, JP-A-10-502737,JP-A-2007-511645, JP-A-2008-500437 and JP-A-2008-531836.

The odor masking agent may be known perfumes which have been used for aheat cycle system together with a working fluid comprising a halogenatedhydrocarbon, such as perfumes as disclosed in e.g. JP-A-2008-500437 andJP-A-2008-531836.

In a case where the leak detecting substance is used, a solubilizingagent which improves the solubility of the leak detecting substance inthe working fluid may be used.

The solubilizing agent may be ones as disclosed in e.g.JP-A-2007-511645, JP-A-2008-500437 and JP-A-2008-531836.

The content of the leak detecting substance in the composition for aheat cycle system is not particularly limited within a range not toremarkably decrease the effects of the present invention, and ispreferably at most 2 parts by the mass, more preferably at most 0.5 partby the mass per 100 parts by the mass of the working fluid.

[Heat Cycle System]

The heat cycle system of the present invention is a system employing thecomposition for a heat cycle system of the present invention. The heatcycle system of the present invention may be a heat pump systemutilizing heat obtained by a condenser or may be a refrigerating cyclesystem utilizing coldness obtained by an evaporator.

The heat cycle system of the present invention may, for example, bespecifically a refrigerator, an air-conditioning apparatus, a powergeneration system, a heat transfer apparatus and a secondary coolingmachine. Among them, the heat cycle system of the present invention,which efficiently exhibits heat cycle performance in a workingenvironment at higher temperature, is preferably employed as anair-conditioning apparatus to be disposed outdoors in many cases.Further, the heat cycle system of the present invention is preferablyemployed also for a refrigerator.

The air-conditioning apparatus may, for example, be specifically a roomair-conditioner, a package air-conditioner (such as a store packageair-conditioner, a building package air-conditioner or a plant packageair-condition, a gas engine heat pump, a train air-conditioning systemor an automobile air-conditioning system.

The refrigerator may, for example, be specifically a showcase (such as abuilt-in showcase or a separate showcase), an industrial fridge freezer,a vending machine or an ice making machine.

The power generation system is preferably a power generation system byRankine cycle system.

The power generation system may, for example, be specifically a systemwherein in an evaporator, a working fluid is heated by e.g. geothermalenergy, solar heat or waste heat in a medium-to-high temperature rangeat a level of from 50 to 200° C., and the vaporized working fluid in ahigh temperature and high pressure state is adiabatically expanded by anexpansion device, so that a power generator is driven by the workgenerated by the adiabatic expansion to carry out power generation.

Further, the heat cycle system of the present invention may be a heattransport apparatus. The heat transport apparatus is preferably a latentheat transport apparatus.

The latent heat transport apparatus may, for example, be a heat pipeconducting latent heat transport utilizing evaporation, boiling,condensation, etc. of a working fluid filled in an apparatus, and atwo-phase closed thermosiphon. A heat pipe is applied to a relativelysmall-sized cooling apparatus such as a cooling apparatus of a heatingportion of a semiconductor device and electronic equipment. A two-phaseclosed thermosiphon is widely used for a gas/gas heat exchanger, toaccelerate snow melting and to prevent freezing of roads, since it doesnot require a wick and its structure is simple.

Now, as an example of the heat cycle system according the embodiment ofthe present invention, a refrigerating cycle system will be describedwith reference to a refrigerating cycle system 10 which has been roughlydescribed above, of which the schematic construction view is shown inFIG. 1, as an example. A refrigerating cycle system is a systemutilizing coldness obtained by an evaporator.

A refrigerating cycle system 10 shown in FIG. 1 is a system generallycomprising a compressor 11 to compress a working fluid vapor A to form ahigh temperature/high pressure working fluid vapor B, a condenser 12 tocool and liquefy the working fluid vapor B discharged from thecompressor 11 to form a low temperature/high pressure working fluid C,an expansion valve 13 to let the working fluid C discharged from thecondenser 12 expand to form a low temperature/low pressure working fluidD, an evaporator 14 to heat the working fluid D discharged from theexpansion valve 13 to form a high temperature/low pressure working fluidvapor A, a pump 15 to supply a load fluid E to the evaporator 14, and apump 16 to supply a fluid F to the condenser 12.

In the refrigerating cycle system 10, a cycle of the following (i) to(iv) is repeated.

(i) A working fluid vapor A discharged from an evaporator 14 iscompressed by a compressor 11 to form a high temperature/high pressureworking fluid vapor B (hereinafter referred to as “AB process”).

(ii) The working fluid vapor B discharged from the compressor 11 iscooled and liquefied by a fluid F in a condenser 12 to form a lowtemperature/high pressure working fluid C. At that time, the fluid F isheated to form a fluid F′, which is discharged from the condenser 12(hereinafter referred to as “BC process”).

(iii) The working fluid C discharged from the condenser 12 is expandedin an expansion valve 13 to form a low temperature/low pressure workingfluid D (hereinafter referred to as “CD process”).

(iv) The working fluid D discharged from the expansion valve 13 isheated by a load fluid E in the evaporator 14 to form a hightemperature/low pressure working fluid vapor A. At that time, the loadfluid E is cooled and becomes a load fluid E′, which is discharged fromthe evaporator 14 (hereinafter referred to as “DA process”).

The refrigerating cycle system 10 is a cycle system comprising anadiabatic isentropic change, an isenthalpic change and an isobaricchange. The state change of the working fluid, as represented on apressure enthalpy chart (curve) as shown in FIG. 2, may be representedas a trapezoid having points A, B, C and D as vertexes.

The AB process is a process wherein adiabatic compression is carried outby the compressor 11 to change the high temperature/low pressure workingfluid vapor A to a high temperature/high pressure working fluid vapor B,and is represented by the line AB in FIG. 2.

The BC process is a process wherein isobaric cooling is carried out inthe condenser 12 to change the high temperature/high pressure workingfluid vapor B to a low temperature/high pressure working fluid C and isrepresented by the BC line in FIG. 2. The pressure in this process isthe condensation pressure. Of the two intersection points of thepressure enthalpy chart and the BC line, the intersection point T₁ onthe high enthalpy side is the condensing temperature, and theintersection point T₂ on the low enthalpy side is the condensationboiling point temperature. Here, in a case where the working fluid is asingle compound or an azeotropic mixture, T₁ and T₂ are equal to eachother. In a case where the working fluid is a non-azeotropic mixture, T₁and T₂ are different from each other. In the present invention, in sucha case, the higher temperature between T₁ and T₂ is taken as the“condensing temperature”. Further, the temperature glide in the case ofa non-azeotropic mixture fluid is represented by the difference betweenT₁ and T₂.

The CD process is a process wherein isenthalpic expansion is carried outby the expansion valve 13 to change the low temperature/high pressureworking fluid C to a low temperature/low pressure working fluid D and ispresented by the CD line in FIG. 2. T₂-T₃ corresponds to thesupercoiling degree (hereinafter referred to as “SC” as the caserequires) of the working fluid in the cycle of (i) to (iv), where T₃ isthe temperature of the low temperature/high pressure working fluid C.

The DA process is a process wherein isobaric heating is carried out inthe evaporator 14 to have the low temperature/low pressure working fluidD returned to a high temperature/low pressure working fluid vapor A, andis represented by the DA line in FIG. 2. The pressure in this process isthe evaporation pressure. Of the two intersection points of the pressureenthalpy chart and the DA line, the intersection point T₆ on the highenthalpy side is the evaporation temperature. T₇−T₆ corresponds to thedegree of superheat (hereinafter referred to as “SH” as the caserequires) of the working fluid in the cycle of (i) to (iv), where T₇ isthe temperature of the working fluid vapor A. T₄ indicates thetemperature of the working fluid D. Here, in a case where the workingfluid is a single compound or an azeotropic mixture, T₄ and T₆ are equalto each other. In a case where the working fluid is a non-azeotropicmixture, T₄ and T₆ are different from each other. In the presentinvention, in such a case, the lower temperature between T₄ and T₆ istaken as the “evaporation temperature”.

Here, cycle performance of the working fluid is evaluated, for example,by the refrigerating capacity (hereinafter referred to as “Q” as thecase requires) and the coefficient of performance (hereinafter referredto as “COP” as the case requires) of the working fluid. Q and COP of theworking fluid are obtained respectively in accordance with the followingformulae (A) and (B) from enthalpies h_(A), h_(B), h_(C) and h_(D) inthe respective states A (after evaporation, high temperature and lowpressure), B (after compression, high temperature and high pressure), C(after condensation, low temperature and high pressure) and D (afterexpansion, low temperature and low pressure) of the working fluid:Q=h _(A) −h _(D)  (A)COP=Q/compression work=(h _(A) −h _(D))/(h _(B) −h _(A))  (B)

COP means the efficiency in the refrigerating cycle system, and a higherCOP means that a higher output, for example, Q, can be obtained by asmaller input, for example, an electric energy required to operate acompressor.

Further, Q means a capacity to freeze a load fluid, and a higher Q meansthat more works can be done in the same system. In other words, it meansthat with a working fluid having a higher Q, the desired performance canbe obtained with a smaller amount, whereby the system can be downsized.

In the heat cycle system of the present invention employing thecomposition for a heat cycle system of the present invention, in arefrigerating cycle system 10 shown in FIG. 1 for example, as comparedwith a case where R410 (a mixed fluid of HFC-32 and HFC-125 in a massratio of 1:1) which has been commonly used for an air-conditioningapparatus or the like, it is possible to achieve high levels of Q andCOP, i.e. equal to or higher than those of R410A, while remarkablysuppressing the global worming potential.

Further, since the working fluid contained in the composition for a heatcycle system to be employed may have a composition with which thetemperature glide of the working fluid is suppressed to a certain levelor lower, and in such a case, the composition change when thecomposition for a heat cycle system is put into a refrigerator or anair-conditioning apparatus from a pressure container and a change in therefrigerant composition in a refrigerator or an air-conditioningapparatus when the refrigerant leaks out from the refrigerator or theair-conditioning apparatus, can be suppressed to lower levels. Further,according to the composition for a heat cycle system of the presentinvention, the lubricating properties of the fluorinated hydrocarboncompound contained as the working fluid are improved, and accordingly aheat cycle system employing the composition can maintain a moreefficient circulation state of the working fluid as compared with aconventional system, and can be stably operated.

In the heat cycle system, as described above, since the working fluidused in the present invention contains a carbon-carbon double bond, theworking fluid may be decomposed to generate an acid at the time ofoperation of the system. In the present invention, a refrigerant oil isused in combination with the working fluid to suppress generation of anacid, however, it is preferred to constitute the heat cycle system so asto be stably operated even if an acid is generated by some reasons.

That is, the contact portion to be in contact with the composition for aheat cycle system is preferably composed of at least one member selectedfrom an engineering plastic, an organic film and an inorganic film. Asthe contact portion, particularly, a slide member in a case where thesystem has a compression mechanism, a sealing member in the interior ofthe heat cycle system, and the like, may be mentioned as members to beprotected. More particularly, a slide member (such as a bearing)provided at a slide portion of a compressor, a sealing member to preventleakage of the working fluid from the compressor, an insulating materialprovided on an electric motor, etc. may be mentioned.

The engineering plastic used is preferably at least one member selectedfrom a polyamide resin, a polyphenylene sulfide resin, a polyacetalresin and a fluororesin.

Further, the organic film used is preferably at least one film selectedfrom a polytetrafluoroethylene-coated film, a polyimide-coated film, apolyamideimide-coated film, and a thermosetting insulating film formedby using a resin coating composition containing a resin comprising apolyhydroxy ether resin and a polysulfone resin, and a crosslinkingagent.

Further, the inorganic film used is at least one film selected from agraphite film, a diamond-like carbon film, a tin film, a chromium film,a nickel film and a molybdenum film.

Further, in a case where the contact portion is a slide member, forexample, it is preferred to use any one of polytetrafluoroethylene,polyphenylene sulfide and polyamide, and in a case where it is a sealingportion, for example, it is preferably made of at least one memberselected from polytetrafluoroethylene, polyphenylene sulfide,chloroprene rubber, silicon rubber, hydrogenated nitrile rubber,fluorocarbon rubber and epichlorohydrin rubber.

Further, as the insulating material of an electric motor, an insulatingcovering material for a stator coil, an insulating film and the like maybe mentioned. Such an insulating covering material and an insulatingfilm are made of a resin which will not be degenerated physically orchemically, even when brought into contact with a working fluid at hightemperature under high pressure, by the working fluid, particularly aresin having solvent resistance, extraction resistance, thermal/chemicalstability and bubbling resistance.

Specifically, for an insulating covering material for a stator coil, anyone of polyvinyl formal, polyester, THEIC-modified polyester, polyimide,polyamideimide, polyesterimide and polyesteramideimide is used.Preferred is a double coated wire consisting of polyamideimide as anupper layer and polyesterimide as a lower layer. Further, in addition tothe above material, an enamel covering with a glass transitiontemperature of at least 120° C. may be used.

Further, for an insulating film, any one of polyethylene terephthalate(PET), polyethylene naphthalate (PEN), polyphenylene sulfide (PPS) andpolybutylene terephthalate (PBT) is used. Further, for the insulatingfilm, it is possible to use a foamed film of which the foamed materialis the same as the working fluid for a refrigerating cycle. For aninsulating material to hold a coil such as an insulator, polyether etherketone (PEEK) or a liquid crystal polymer (LCP) is used. For varnish, anepoxy resin is used.

At the time of operation of the heat cycle system, in order to avoiddrawbacks due to inclusion of moisture or inclusion of non-condensinggas such as oxygen, it is preferred to provide a means to suppress suchinclusion.

If moisture is included in the heat cycle system, a problem may occurparticularly when the heat cycle system is used at low temperature. Forexample, problems such as freezing in a capillary tube, hydrolysis ofthe working fluid or the refrigerant oil, deterioration of materials byan acid component formed in the cycle, formation of contaminants, etc.may arise. Particularly, if the refrigerant oil is a polyglycolrefrigerant oil or a polyol ester refrigerant oil, it has extremely highmoisture absorbing properties and is likely to undergo hydrolysis, andinclusion of moisture decreases properties of the refrigerant oil andmay be a great cause to impair the long term reliability of acompressor. Accordingly, in order to suppress hydrolysis of therefrigerant oil, it is necessary to control the moisture concentrationin the heat cycle system.

As a method of controlling the moisture concentration in the heat cyclesystem, a method of using a moisture-removing means such as adesiccating agent (such as silica gel, activated aluminum or zeolite)may be mentioned. The desiccating agent is preferably brought intocontact with the composition for a heat cycle system in a liquid state,in view of the dehydration efficiency. For example, the desiccatingagent is located at the outlet of the condenser 12 or at the inlet ofthe evaporator 14 to be brought into contact with the composition for aheat cycle system.

The desiccating agent is preferably a zeolite desiccating agent in viewof chemical reactivity of the desiccating agent and the composition fora heat cycle system, and the moisture absorption capacity of thedesiccating agent.

The zeolite desiccating agent is, in a case where a refrigerant oilhaving a large moisture absorption as compared with a conventionalmineral refrigerant oil is used, preferably a zeolite desiccating agentcontaining a compound represented by the following formula (C) as themain component in view of excellent moisture absorption capacity.M_(2/n)O.Al₂O₃ .xSiO₂ .yH₂O  (C)wherein M is a group 1 element such as Na or K or a group 2 element suchas Ca, n is the valence of M, and x and y are values determined by thecrystal structure. The pore size can be adjusted by changing M.

To select the desiccating agent, the pore size and the fracture strengthare important.

In a case where a desiccating agent having a pore size larger than themolecular size of the working fluid and the refrigerant oil contained inthe composition for a heat cycle system is used, the working fluid andthe refrigerant oil is adsorbed in the desiccating agent and as aresult, chemical reaction between the working fluid and the refrigerantoil and the desiccating agent will occur, thus leading to undesiredphenomena such as formation of non-condensing gas, a decrease in thestrength of the desiccating agent, and a decrease in the adsorptioncapacity.

Accordingly, it is preferred to use as the desiccating agent a zeolitedesiccating agent having a small pore size. Particularly preferred issodium/potassium type A synthetic zeolite having a pore size of at most3.5 Å. By using a sodium/potassium type A synthetic zeolite having apore size smaller than the molecular size of the working fluid and therefrigerant oil, it is possible to selectively adsorb and remove onlymoisture in the heat cycle system without adsorbing the working fluidand the refrigerant oil. In other words, the working fluid and therefrigerant oil are less likely to be adsorbed in the desiccating agent,whereby heat decomposition is less likely to occur and as a result,deterioration of materials constituting the heat cycle system andformation of contaminants can be suppressed.

The size of the zeolite desiccating agent is preferably from about 0.5to about 5 mm, since if it is too small, a valve or a thin portion inpipelines of the heat cycle system may be clogged, and if it is toolarge, the drying capacity will be decreased. Its shape is preferablygranular or cylindrical.

The zeolite desiccating agent may be formed into an optional shape bysolidifying powdery zeolite by a binding agent (such as bentonite). Solong as the desiccating agent is composed mainly of the zeolitedesiccating agent, other desiccating agent (such as silica gel oractivated alumina) may be used in combination.

The proportion of the zeolite desiccating agent based on the compositionfor a heat cycle system is not particularly limited.

If non-condensing gas is included in the heat cycle system, it hasadverse effects such as heat transfer failure in the condenser or theevaporator and an increase in the working pressure, and it is necessaryto suppress its inclusion as far as possible. Particularly, oxygen whichis one of non-condensing gases reacts with the working fluid or therefrigerant oil and promotes their decomposition.

The non-condensing gas concentration is preferably at most 1.5 vol %,particularly preferably at most 0.5 vol % by the volume ratio based onthe working fluid, in a gaseous phase of the working fluid.

According to the above-described heat cycle system of the presentinvention, which employs the composition for a heat cycle system of thepresent invention, favorable lubricating properties are achieved,practically sufficient heat cycle performance can be obtained whilesuppressing influence over global warming, and there is substantially noproblem with respect to the temperature glide.

EXAMPLES

Now, the present invention will be described in further detail withreference to Examples of the present invention, conventional Examplesand Comparative Examples. In each Ex., one of the following workingfluids 1 to 64 and one of the following refrigerant oils A to I wereselected, 50 g of the working fluid and 50 g of the refrigerant oil weremixed and dissolved to prepare 576 types of composition for a heat cyclesystem. Accordingly, the composition for a heat cycle system in Ex. isone comprising 50 mass % of the working fluid and 50 mass % of therefrigerant oil. Further, for some working fluids, an antioxidant wasadded to constitute the composition for a heat cycle system, asdescribed hereinafter.

The following working fluids and refrigerant oils were used. Compoundsconstituting the working fluids are shown in Table 2, and compoundsconstituting the refrigerant oils are shown in Table 3.

TABLE 2 mass % Working fluid HFO-1123 HFC-32 HFO-1234yf HFC-134aHFC-152a HFC-125 1 100 2 20 80 3 40 60 4 50 50 5 60 40 6 80 20 7 30 4030 8 50 50 9 50 50 10 50 50 11 50 50 12 50 40 10 13 40 40 20 14 20 40 4015 10 40 50 16 40 50 10 17 30 50 20 18 20 50 30 19 10 50 40 20 30 60 1021 20 60 20 22 10 60 30 23 20 70 10 24 10 70 20 25 40 10 50 26 50 10 4027 60 10 30 28 70 10 20 29 80 10 10 30 40 20 40 31 50 20 30 32 60 20 2033 70 20 10 34 60 30 10 35 50 30 20 36 40 30 30 37 30 30 40 38 40 55 539 40 45 15 40 40 35 25 41 45 50 5 42 45 45 10 43 45 40 15 44 45 35 2045 45 30 25 46 45 25 30 47 50 45 5 48 50 35 15 49 50 25 25 50 55 40 5 5155 35 10 52 55 30 15 53 55 25 20 54 55 20 25 55 55 15 30 56 30 45 25 5730 55 15 58 30 65 5 59 35 35 30 60 35 40 25 61 35 45 20 62 35 50 15 6335 55 10 64 35 60 5 Refrigerant oil A: polyol ester refrigerant oil(tradename: UNISTER RH-208BRS, manufactured by NOF CORPORATION)Refrigerant oil B: polyol ester refrigerant oil (tradename: UNISTERRH-481 R, manufactured by NOF CORPORATION) Refrigerant oil C: polyolester refrigerant oil (tradename: UNISTER RHR-32, manufactured by NOFCORPORATION) Refrigerant oil D: polyol ester refrigerant oil (tradename:UNISTER RHR-64, manufactured by NOF CORPORATION) Refrigerant oil E:polyol ester refrigerant oil (tradename: UNISTER RHR-200, manufacturedby NOF CORPORATION) Refrigerant oil F: polyol ester refrigerant oil(tradename: UNISTER RHR-609BR, manufactured by NOF CORPORATION)Refrigerant oil G: refrigerant oil containing a polyol ester as the maincomponent (tradename: Ze-GLES RB-68, manufactured by J X Nippon Oil &Energy Corporation) Refrigerant oil H: refrigerant oil containing apolyvinyl ether as the main component (tradename: Daphne Hermetic OilFVC68D, manufactured by Idemitsu Kosan Co., Ltd.) Refrigerant oil I:naphthene type higher refrigerant oil (tradename: SUNISO 4GS,manufactured by Idemitsu Kosan Co., Ltd.)

TABLE 3 Hydroxy Kinematic Refrigerant value Flash viscosity ViscosityPour Breakdown oil: mg point (mm²/s) index point voltage tradename KOH/g[° C.] 40° C. 100° C. [—] [° C.] [kV] A UNISTER 0.10 168 8 2 52 −50 >25RH-208BRS B UNISTER 0.50 330 65 12 191 −20 >50 RH-481R C UNISTER 0.10273 34 6 114 −50 >50 RHR-32 D UNISTER 0.10 283 65 9 113 −38 >50 RHR-64 EUNISTER 0.10 298 235 18 81 −30 >25 RHR-200 F UNISTER 0.30 302 462 28 85−18 >25 RHR-609BR G Ze-GLES 0.01 255 65 8 90 −40 >50 RB-68 H FVC68D 0.01206 66 8 84 −37 74 I 4GS 0.00 188 54 6 — −35 50

Further, for each of the refrigerant oils A to F, as an additive, anantioxidant (2,6-di-tert-butyl-4-methylphenol) was added in an amount of0.5 mass % per 100 mass % of the total amount of the refrigerant oil andthe antioxidant, to form a refrigerant oil composition, which was usedfor production and was evaluated. In the following test examples, evenin a case where such a refrigerant oil composition was used, therefrigerant oil composition was represented as “refrigerant oil”.

[Tests]

(Compatibility with Working Fluid)

Using the above-described working fluid and refrigerant oil, thecompatibility of each test oil with the working fluid was evaluated inaccordance with the method of test for the determination ofcompatibility with refrigerant in JIS K 2211 “Refrigerant oils”. Theworking fluid and the refrigerant oil were blended in a proportion ofthe refrigerant oil of 15 mass %, and the phase separation state wasvisually confirmed at −60° C. and at 35° C. and evaluated based on thefollowing standards.

◯: The working fluid and the refrigerant oil were compatible with eachother at both temperatures.

Δ: The working fluid and the refrigerant oil became turbid at bothtemperatures.

X: The working fluid and the refrigerant oil were separated from eachother at both temperatures.

(Aniline Point of Refrigerant Oil)

Using the above refrigerant oil, the aniline point of each test oil wasevaluated in accordance with JIS K2256 “Petroleum products-determinationof aniline point and mixed aniline point”. Aniline and the refrigerantoil were blended in a mass ratio of 50 mass %:50 mass %, the obtainedmixture was cooled from 0° C. to −100° C., and the phase separationstate was visually confirmed and evaluated based on the followingstandards.

◯: There was an aniline point within a range of from −100 to 0° C.

x: There was no aniline point within a range of from −100 to 0° C.

(Weight Change by Immersion Test)

The test was carried out in accordance with JIS K7114 “Plastics-Methodsof test for the determination of the effects of immersion in liquidchemicals”. The composition for a heat cycle system was put in a 200 mlstainless steel pressure resistant container in which a 150 ml glasstube was put, and about 10 g of a nylon-11 test specimen was put, andthe container was closed. Then, the closed pressure resistant containerwas stored in a constant temperature chamber (perfect oven PHH-202,manufactured by ESPEC CORP.) at 175° C. for 14 days, and the weightchange of the test specimen was confirmed and evaluated based on thefollowing standards.

◯: No mass change of 1% or more.

x: Mass change of 1% or more confirmed.

A mass change indicates that the resin swelled by the immersion test.

(Circulation State of Refrigerant Oil)

Each composition for a heat cycle system was introduced into a heatcycle system 10 shown in FIG. 1, and the heat cycle system wascontinuously operated. To evaluate the circulation state of thecomposition for a heat cycle system, part of a flow path from anevaporator 14 to a compressor 11 in the heat cycle system wasconstituted by a glass pipe. Through the glass pipe, the interior wasobserved to evaluate the circulation state of the composition for a heatcycle system in the heat cycle system. The circulation state wasvisually evaluated based on the following standards.

◯: Circulation of the refrigerant oil was confirmed.

Δ: Although circulation of the refrigerant oil was confirmed, thecirculation amount was slightly small.

x: Circulation of the refrigerant oil was not confirmed.

(Stability Test)

The stability test was carried out in accordance with the method of testfor chemical stability of refrigerant and refrigerant oil (autoclave)described in JIS K2211. The composition for a heat cycle system was putin a 200 ml stainless steel pressure resistant container in which a 150ml glass tube was put, and as a catalyst, iron, copper and aluminum testspecimens were put in one pressure resistant container, and thecontainer was closed. Then, the closed pressure resistant container wasstored in a constant temperature chamber (perfect oven PHH-202,manufactured by ESPEC CORP.) at 175° C. for 14 days, and the acidcontent in the working fluid was measured, the hue of the refrigerantoil was observed, and a change of the outer appearance of the catalystwas observed, as follows.

Further, as the metal specimens as the catalyst, the following wereused.

a) Iron: a test specimen of cold-reduced carbon steel sheet (asstipulated in JIS G3141, SPCC-SB), 30 mm×25 mm×3.2 mm in thickness

b) Copper: a test specimen of tough pitch copper (as stipulated in JISH3100, alloy number C1100, C1100P), 30 mm×25 mm×2 mm in thickness

c) Aluminum: a test specimen of pure aluminum (as stipulated in JISH4000, alloy number 1050, A1050P), 30 mm×25 mm×2 mm in thickness

(Hue of Refrigerant Oil)

After the stability test, the refrigerant oil remaining in the pressureresistant container from which the working fluid had been withdrawn, wastaken out, and the hue of the refrigerant oil was evaluated inaccordance with ASTM-D156.

◯: No change observed.

X: Coloring proceeded.

In a case where coloring proceeded, the composition for a heat cyclesystem was deteriorated by the stability test.

(Change of Outer Appearance of Catalyst)

The outer appearance of the catalyst metal after the stability test wasvisually confirmed, and the change of the outer appearance of thecatalyst was evaluated based on the following standards.

◯: No change was confirmed.

x: Gloss of the catalyst disappeared or the catalyst blackened.

In a case where the gloss of the catalyst disappeared or the catalystblackened, the composition for a heat cycle system was deteriorated bythe stability test.

(Sludge)

Presence or absence of sludge was evaluated based on the followingstandards by visually observing the container after the stability test.

◯: No sludge observed.

X: Sludge observed.

In a case where sludge was observed, the composition for a heat cyclesystem underwent decomposition of some kind or polymerization reactionby the stability test.

[Test Results]

(Compatibility with Working Fluid)

The results are shown in Tables 4 and 5. Only the refrigerant oil I wasseparated from the working fluid, and favorable compatibility of polyolester and polyvinyl ether refrigerant oils was confirmed. However, noremarkable difference among the types of the working fluid wasconfirmed, and the same result as the working fluid 11 (R-410A) which isa commercially available composition was obtained. However, refrigerantoils E and F which had a high kinematic viscosity tended to becometurbid even though they were polyol ester type.

TABLE 4 Working Refrigerant oil fluid A B C D E F G H I 1 ◯ ◯ ◯ ◯ Δ Δ ◯◯ X 2 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 3 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 4 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 5 ◯ ◯ ◯◯ Δ Δ ◯ ◯ X 6 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 7 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 8 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X9 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 10 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 11 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 12 ◯ ◯ ◯ ◯Δ Δ ◯ ◯ X 13 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 14 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 15 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X16 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 17 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 18 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 19 ◯ ◯ ◯◯ Δ Δ ◯ ◯ X 20 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 21 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 22 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯X 23 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 24 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 25 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 26 ◯ ◯◯ ◯ Δ Δ ◯ ◯ X 27 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 28 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 29 ◯ ◯ ◯ ◯ Δ Δ ◯◯ X 30 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 31 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 32 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X

TABLE 5 Working Refrigerant oil fluid A B C D E F G H I 33 ◯ ◯ ◯ ◯ Δ Δ ◯◯ X 34 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 35 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 36 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 37 ◯◯ ◯ ◯ Δ Δ ◯ ◯ X 38 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 39 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 40 ◯ ◯ ◯ ◯ Δ Δ◯ ◯ X 41 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 42 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 43 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 44◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 45 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 46 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 47 ◯ ◯ ◯ ◯ ΔΔ ◯ ◯ X 48 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 49 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 50 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X51 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 52 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 53 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 54 ◯ ◯ ◯◯ Δ Δ ◯ ◯ X 55 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 56 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 57 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯X 58 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 59 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 60 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 61 ◯ ◯◯ ◯ Δ Δ ◯ ◯ X 62 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 63 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 64 ◯ ◯ ◯ ◯ Δ Δ ◯◯ X(Aniline Point of Refrigerant Oil)

The results are shown in Table 6. Only the refrigerant oil I had ananiline point at 80° C., and a definite difference from the polyol esterand polyvinyl ether refrigerant oils was confirmed.

TABLE 6 Refrigerant oil Evaluation A ◯ B ◯ C ◯ D ◯ E ◯ F ◯ G ◯ H ◯ I X(Weight Change by Immersion Test)

The results are shown in Tables 7 and 8. A weight change occurred onlyin the refrigerant oil I having no aniline point at from −100 to 0° C.,and a definite difference from the polyol ester and polyvinyl etherrefrigerant oils was confirmed. However, no remarkable difference amongthe types of the working fluid was confirmed, and the same result as theworking fluid 11 (R-410A) which is a commercially available compositionwas obtained.

TABLE 7 Working Refrigerant oil fluid A B C D E F G H I 1 ◯ ◯ ◯ ◯ ◯ ◯ ◯◯ X 2 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 3 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 4 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 5 ◯ ◯ ◯◯ ◯ ◯ ◯ ◯ X 6 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 7 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 8 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X9 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 10 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 11 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 12 ◯ ◯ ◯ ◯◯ ◯ ◯ ◯ X 13 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 14 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 15 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X16 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 17 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 18 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 19 ◯ ◯ ◯◯ ◯ ◯ ◯ ◯ X 20 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 21 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 22 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯X 23 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 24 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 25 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 26 ◯ ◯◯ ◯ ◯ ◯ ◯ ◯ X 27 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 28 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 29 ◯ ◯ ◯ ◯ ◯ ◯ ◯◯ X 30 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 31 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 32 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X

TABLE 8 Working Refrigerant oil fluid A B C D E F G H I 33 ◯ ◯ ◯ ◯ ◯ ◯ ◯◯ X 34 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 35 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 36 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 37 ◯◯ ◯ ◯ ◯ ◯ ◯ ◯ X 38 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 39 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 40 ◯ ◯ ◯ ◯ ◯ ◯◯ ◯ X 41 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 42 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 43 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 44◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 45 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 46 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 47 ◯ ◯ ◯ ◯ ◯◯ ◯ ◯ X 48 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 49 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 50 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X51 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 52 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 53 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 54 ◯ ◯ ◯◯ ◯ ◯ ◯ ◯ X 55 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 56 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 57 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯X 58 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 59 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 60 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 61 ◯ ◯◯ ◯ ◯ ◯ ◯ ◯ X 62 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 63 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ X 64 ◯ ◯ ◯ ◯ ◯ ◯ ◯◯ X(Circulation State of Refrigerant Oil)

The results are shown in Tables 9 and 10. No sufficient flow amount wasconfirmed only with the refrigerant oil I, and a definite differencefrom the polyol ester and polyvinyl ether refrigerant oils wasconfirmed. However, no remarkable difference among the types of theworking fluid was confirmed, and the same result as the working fluid 11(R-410A) which is a commercially available composition was obtained.However, with the refrigerant oils E and F which had a high kinematicviscosity, even though they are polyol ester type, the circulationamount tended to be slightly small.

TABLE 9 Working Refrigerant oil fluid A B C D E F G H I 1 ◯ ◯ ◯ ◯ Δ Δ ◯◯ X 2 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 3 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 4 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 5 ◯ ◯ ◯◯ Δ Δ ◯ ◯ X 6 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 7 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 8 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X9 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 10 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 11 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 12 ◯ ◯ ◯ ◯Δ Δ ◯ ◯ X 13 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 14 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 15 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X16 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 17 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 18 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 19 ◯ ◯ ◯◯ Δ Δ ◯ ◯ X 20 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 21 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 22 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯X 23 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 24 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 25 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 26 ◯ ◯◯ ◯ Δ Δ ◯ ◯ X 27 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 28 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 29 ◯ ◯ ◯ ◯ Δ Δ ◯◯ X 30 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 31 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 32 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X

TABLE 10 Working Refrigerant oil fluid A B C D E F G H I 33 ◯ ◯ ◯ ◯ Δ Δ◯ ◯ X 34 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 35 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 36 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 37◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 38 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 39 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 40 ◯ ◯ ◯ ◯ ΔΔ ◯ ◯ X 41 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 42 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 43 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X44 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 45 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 46 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 47 ◯ ◯ ◯◯ Δ Δ ◯ ◯ X 48 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 49 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 50 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯X 51 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 52 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 53 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 54 ◯ ◯◯ ◯ Δ Δ ◯ ◯ X 55 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 56 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 57 ◯ ◯ ◯ ◯ Δ Δ ◯◯ X 58 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 59 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 60 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 61 ◯◯ ◯ ◯ Δ Δ ◯ ◯ X 62 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 63 ◯ ◯ ◯ ◯ Δ Δ ◯ ◯ X 64 ◯ ◯ ◯ ◯ Δ Δ◯ ◯ X[Stability Test]

The stability test was conducted on the refrigerant oils except for therefrigerant oil I with which no sufficient flow amount could bemaintained.

(Hue of Refrigerant Oil)

The results are shown in Tables 11 and 12. Favorable results wereobtained with respect to all the combinations of the working fluidsexcept for the working fluid 11 (R-410A) and the refrigerant oils A, Cto E and G to H. A remarkable progress of coloring was confirmed withrespect to the combinations with the refrigerant oils B and F.

TABLE 11 Working Refrigerant oil fluid A B C D E F G H 1 ◯ X ◯ ◯ ◯ X ◯ ◯2 ◯ X ◯ ◯ ◯ X ◯ ◯ 3 ◯ X ◯ ◯ ◯ X ◯ ◯ 4 ◯ X ◯ ◯ ◯ X ◯ ◯ 5 ◯ X ◯ ◯ ◯ X ◯ ◯6 ◯ X ◯ ◯ ◯ X ◯ ◯ 7 ◯ X ◯ ◯ ◯ X ◯ ◯ 8 ◯ X ◯ ◯ ◯ X ◯ ◯ 9 ◯ X ◯ ◯ ◯ X ◯ ◯10 ◯ X ◯ ◯ ◯ X ◯ ◯ 11 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ 12 ◯ X ◯ ◯ ◯ X ◯ ◯ 13 ◯ X ◯ ◯ ◯ X◯ ◯ 14 ◯ X ◯ ◯ ◯ X ◯ ◯ 15 ◯ X ◯ ◯ ◯ X ◯ ◯ 16 ◯ X ◯ ◯ ◯ X ◯ ◯ 17 ◯ X ◯ ◯◯ X ◯ ◯ 18 ◯ X ◯ ◯ ◯ X ◯ ◯ 19 ◯ X ◯ ◯ ◯ X ◯ ◯ 20 ◯ X ◯ ◯ ◯ X ◯ ◯ 21 ◯ X◯ ◯ ◯ X ◯ ◯ 22 ◯ X ◯ ◯ ◯ X ◯ ◯ 23 ◯ X ◯ ◯ ◯ X ◯ ◯ 24 ◯ X ◯ ◯ ◯ X ◯ ◯ 25◯ X ◯ ◯ ◯ X ◯ ◯ 26 ◯ X ◯ ◯ ◯ X ◯ ◯ 27 ◯ X ◯ ◯ ◯ X ◯ ◯ 28 ◯ X ◯ ◯ ◯ X ◯ ◯29 ◯ X ◯ ◯ ◯ X ◯ ◯ 30 ◯ X ◯ ◯ ◯ X ◯ ◯ 31 ◯ X ◯ ◯ ◯ X ◯ ◯ 32 ◯ X ◯ ◯ ◯ X◯ ◯

TABLE 12 Working Refrigerant oil fluid A B C D E F G H 33 ◯ X ◯ ◯ ◯ X ◯◯ 34 ◯ X ◯ ◯ ◯ X ◯ ◯ 35 ◯ X ◯ ◯ ◯ X ◯ ◯ 36 ◯ X ◯ ◯ ◯ X ◯ ◯ 37 ◯ X ◯ ◯ ◯X ◯ ◯ 38 ◯ X ◯ ◯ ◯ X ◯ ◯ 39 ◯ X ◯ ◯ ◯ X ◯ ◯ 40 ◯ X ◯ ◯ ◯ X ◯ ◯ 41 ◯ X ◯◯ ◯ X ◯ ◯ 42 ◯ X ◯ ◯ ◯ X ◯ ◯ 43 ◯ X ◯ ◯ ◯ X ◯ ◯ 44 ◯ X ◯ ◯ ◯ X ◯ ◯ 45 ◯X ◯ ◯ ◯ X ◯ ◯ 46 ◯ X ◯ ◯ ◯ X ◯ ◯ 47 ◯ X ◯ ◯ ◯ X ◯ ◯ 48 ◯ X ◯ ◯ ◯ X ◯ ◯49 ◯ X ◯ ◯ ◯ X ◯ ◯ 50 ◯ X ◯ ◯ ◯ X ◯ ◯ 51 ◯ X ◯ ◯ ◯ X ◯ ◯ 52 ◯ X ◯ ◯ ◯ X◯ ◯ 53 ◯ X ◯ ◯ ◯ X ◯ ◯ 54 ◯ X ◯ ◯ ◯ X ◯ ◯ 55 ◯ X ◯ ◯ ◯ X ◯ ◯ 56 ◯ X ◯ ◯◯ X ◯ ◯ 57 ◯ X ◯ ◯ ◯ X ◯ ◯ 58 ◯ X ◯ ◯ ◯ X ◯ ◯ 59 ◯ X ◯ ◯ ◯ X ◯ ◯ 60 ◯ X◯ ◯ ◯ X ◯ ◯ 61 ◯ X ◯ ◯ ◯ X ◯ ◯ 62 ◯ X ◯ ◯ ◯ X ◯ ◯ 63 ◯ X ◯ ◯ ◯ X ◯ ◯ 64◯ X ◯ ◯ ◯ X ◯ ◯(Change of Outer Appearance of Catalyst)

The results are shown in Tables 13 and 14. In the same manner as the huetest, favorable results were obtained with respect to all thecombinations of the working fluids except for the working fluid 11(R-410A) and the refrigerant oils A, C to E and G to H. A remarkablechange of the outer appearance of the catalyst was confirmed withrespect to the combinations with the refrigerant oils B and F.

TABLE 13 Refrigerant oil Refrigerant A B C D E F G H 1 ◯ X ◯ ◯ ◯ X ◯ ◯ 2◯ X ◯ ◯ ◯ X ◯ ◯ 3 ◯ X ◯ ◯ ◯ X ◯ ◯ 4 ◯ X ◯ ◯ ◯ X ◯ ◯ 5 ◯ X ◯ ◯ ◯ X ◯ ◯ 6◯ X ◯ ◯ ◯ X ◯ ◯ 7 ◯ X ◯ ◯ ◯ X ◯ ◯ 8 ◯ X ◯ ◯ ◯ X ◯ ◯ 9 ◯ X ◯ ◯ ◯ X ◯ ◯ 10◯ X ◯ ◯ ◯ X ◯ ◯ 11 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ 12 ◯ X ◯ ◯ ◯ X ◯ ◯ 13 ◯ X ◯ ◯ ◯ X ◯ ◯14 ◯ X ◯ ◯ ◯ X ◯ ◯ 15 ◯ X ◯ ◯ ◯ X ◯ ◯ 16 ◯ X ◯ ◯ ◯ X ◯ ◯ 17 ◯ X ◯ ◯ ◯ X◯ ◯ 18 ◯ X ◯ ◯ ◯ X ◯ ◯ 19 ◯ X ◯ ◯ ◯ X ◯ ◯ 20 ◯ X ◯ ◯ ◯ X ◯ ◯ 21 ◯ X ◯ ◯◯ X ◯ ◯ 22 ◯ X ◯ ◯ ◯ X ◯ ◯ 23 ◯ X ◯ ◯ ◯ X ◯ ◯ 24 ◯ X ◯ ◯ ◯ X ◯ ◯ 25 ◯ X◯ ◯ ◯ X ◯ ◯ 26 ◯ X ◯ ◯ ◯ X ◯ ◯ 27 ◯ X ◯ ◯ ◯ X ◯ ◯ 28 ◯ X ◯ ◯ ◯ X ◯ ◯ 29◯ X ◯ ◯ ◯ X ◯ ◯ 30 ◯ X ◯ ◯ ◯ X ◯ ◯ 31 ◯ X ◯ ◯ ◯ X ◯ ◯ 32 ◯ X ◯ ◯ ◯ X ◯ ◯

TABLE 14 Refrigerant oil Refrigerant A B C D E F G H 33 ◯ X ◯ ◯ ◯ X ◯ ◯34 ◯ X ◯ ◯ ◯ X ◯ ◯ 35 ◯ X ◯ ◯ ◯ X ◯ ◯ 36 ◯ X ◯ ◯ ◯ X ◯ ◯ 37 ◯ X ◯ ◯ ◯ X◯ ◯ 38 ◯ X ◯ ◯ ◯ X ◯ ◯ 39 ◯ X ◯ ◯ ◯ X ◯ ◯ 40 ◯ X ◯ ◯ ◯ X ◯ ◯ 41 ◯ X ◯ ◯◯ X ◯ ◯ 42 ◯ X ◯ ◯ ◯ X ◯ ◯ 43 ◯ X ◯ ◯ ◯ X ◯ ◯ 44 ◯ X ◯ ◯ ◯ X ◯ ◯ 45 ◯ X◯ ◯ ◯ X ◯ ◯ 46 ◯ X ◯ ◯ ◯ X ◯ ◯ 47 ◯ X ◯ ◯ ◯ X ◯ ◯ 48 ◯ X ◯ ◯ ◯ X ◯ ◯ 49◯ X ◯ ◯ ◯ X ◯ ◯ 50 ◯ X ◯ ◯ ◯ X ◯ ◯ 51 ◯ X ◯ ◯ ◯ X ◯ ◯ 52 ◯ X ◯ ◯ ◯ X ◯ ◯53 ◯ X ◯ ◯ ◯ X ◯ ◯ 54 ◯ X ◯ ◯ ◯ X ◯ ◯ 55 ◯ X ◯ ◯ ◯ X ◯ ◯ 56 ◯ X ◯ ◯ ◯ X◯ ◯ 57 ◯ X ◯ ◯ ◯ X ◯ ◯ 58 ◯ X ◯ ◯ ◯ X ◯ ◯ 59 ◯ X ◯ ◯ ◯ X ◯ ◯ 60 ◯ X ◯ ◯◯ X ◯ ◯ 61 ◯ X ◯ ◯ ◯ X ◯ ◯ 62 ◯ X ◯ ◯ ◯ X ◯ ◯ 63 ◯ X ◯ ◯ ◯ X ◯ ◯ 64 ◯ X◯ ◯ ◯ X ◯ ◯(Sludge)

The results are shown in Tables 15 and 16. In the same manner as the huetest, favorable results were obtained with respect to all thecombinations of the working fluids except for the working fluid 11(R-410A) and the refrigerant oils A, C to E and G to H. A remarkablesludge was confirmed with respect to the combinations with therefrigerant oils B and F.

TABLE 15 Working Refrigerant oil fluid A B C D E F G H 1 ◯ X ◯ ◯ ◯ X ◯ ◯2 ◯ X ◯ ◯ ◯ X ◯ ◯ 3 ◯ X ◯ ◯ ◯ X ◯ ◯ 4 ◯ X ◯ ◯ ◯ X ◯ ◯ 5 ◯ X ◯ ◯ ◯ X ◯ ◯6 ◯ X ◯ ◯ ◯ X ◯ ◯ 7 ◯ X ◯ ◯ ◯ X ◯ ◯ 8 ◯ X ◯ ◯ ◯ X ◯ ◯ 9 ◯ X ◯ ◯ ◯ X ◯ ◯10 ◯ X ◯ ◯ ◯ X ◯ ◯ 11 ◯ ◯ ◯ ◯ ◯ ◯ ◯ ◯ 12 ◯ X ◯ ◯ ◯ X ◯ ◯ 13 ◯ X ◯ ◯ ◯ X◯ ◯ 14 ◯ X ◯ ◯ ◯ X ◯ ◯ 15 ◯ X ◯ ◯ ◯ X ◯ ◯ 16 ◯ X ◯ ◯ ◯ X ◯ ◯ 17 ◯ X ◯ ◯◯ X ◯ ◯ 18 ◯ X ◯ ◯ ◯ X ◯ ◯ 19 ◯ X ◯ ◯ ◯ X ◯ ◯ 20 ◯ X ◯ ◯ ◯ X ◯ ◯ 21 ◯ X◯ ◯ ◯ X ◯ ◯ 22 ◯ X ◯ ◯ ◯ X ◯ ◯ 23 ◯ X ◯ ◯ ◯ X ◯ ◯ 24 ◯ X ◯ ◯ ◯ X ◯ ◯ 25◯ X ◯ ◯ ◯ X ◯ ◯ 26 ◯ X ◯ ◯ ◯ X ◯ ◯ 27 ◯ X ◯ ◯ ◯ X ◯ ◯ 28 ◯ X ◯ ◯ ◯ X ◯ ◯29 ◯ X ◯ ◯ ◯ X ◯ ◯ 30 ◯ X ◯ ◯ ◯ X ◯ ◯ 31 ◯ X ◯ ◯ ◯ X ◯ ◯ 32 ◯ X ◯ ◯ ◯ X◯ ◯

TABLE 16 Working Refrigerant oil fluid A B C D E F G H 33 ◯ X ◯ ◯ ◯ X ◯◯ 34 ◯ X ◯ ◯ ◯ X ◯ ◯ 35 ◯ X ◯ ◯ ◯ X ◯ ◯ 36 ◯ X ◯ ◯ ◯ X ◯ ◯ 37 ◯ X ◯ ◯ ◯X ◯ ◯ 38 ◯ X ◯ ◯ ◯ X ◯ ◯ 39 ◯ X ◯ ◯ ◯ X ◯ ◯ 40 ◯ X ◯ ◯ ◯ X ◯ ◯ 41 ◯ X ◯◯ ◯ X ◯ ◯ 42 ◯ X ◯ ◯ ◯ X ◯ ◯ 43 ◯ X ◯ ◯ ◯ X ◯ ◯ 44 ◯ X ◯ ◯ ◯ X ◯ ◯ 45 ◯X ◯ ◯ ◯ X ◯ ◯ 46 ◯ X ◯ ◯ ◯ X ◯ ◯ 47 ◯ X ◯ ◯ ◯ X ◯ ◯ 48 ◯ X ◯ ◯ ◯ X ◯ ◯49 ◯ X ◯ ◯ ◯ X ◯ ◯ 50 ◯ X ◯ ◯ ◯ X ◯ ◯ 51 ◯ X ◯ ◯ ◯ X ◯ ◯ 52 ◯ X ◯ ◯ ◯ X◯ ◯ 53 ◯ X ◯ ◯ ◯ X ◯ ◯ 54 ◯ X ◯ ◯ ◯ X ◯ ◯ 55 ◯ X ◯ ◯ ◯ X ◯ ◯ 56 ◯ X ◯ ◯◯ X ◯ ◯ 57 ◯ X ◯ ◯ ◯ X ◯ ◯ 58 ◯ X ◯ ◯ ◯ X ◯ ◯ 59 ◯ X ◯ ◯ ◯ X ◯ ◯ 60 ◯ X◯ ◯ ◯ X ◯ ◯ 61 ◯ X ◯ ◯ ◯ X ◯ ◯ 62 ◯ X ◯ ◯ ◯ X ◯ ◯ 63 ◯ X ◯ ◯ ◯ X ◯ ◯ 64◯ X ◯ ◯ ◯ X ◯ ◯

CONCLUSION

It was confirmed that with the composition for a heat cycle systemcomprising a polyol ester or polyvinyl ether refrigerant oil having highcompatibility with a working fluid containing an unsaturated fluorinatedhydrocarbon compound, a sufficient circulation amount which is the sameas the working fluid 11 (R-410A) which is a commercially availablecomposition can be secured, from the results of measurement of thecirculation state. However, from the results of the stability test,coloring of the refrigerant oil, discoloration of the catalyst andformation of sludge were confirmed specifically with respect to thecombinations of the working fluids containing an unsaturated fluorinatedhydrocarbon compound with the refrigerant oils B and F having a highhydroxy value. It is estimated that the double bond contained in theworking fluids except for the working fluid 11 underwent decompositionof some kind or polymerization reaction due to hydroxy groups.Accordingly, it was confirmed that a composition for a heat cycle systemhaving favorable properties can be obtained by using, as a refrigerantoil to be used in combination with a working fluid containing anunsaturated fluorinated hydrocarbon compound having a specificstructure, a refrigerant oil having favorable compatibility with theworking fluid for heat cycle and having a low hydroxy value.

Further, it was confirmed that with the composition for a heat cyclesystem using a polyol ester or polyvinyl ether refrigerant oil havinghigh compatibility with a working fluid containing an unsaturatedfluorinated hydrocarbon compound, and having a kinematic viscosity at40° C. of at most 200 mm²/s, a sufficient circulation amount which isthe same as the working fluid 11 (R-410A) which is a commerciallyavailable composition, can be secured, from the results of measurementof the circulation state.

It was confirmed that with a composition for a heat cycle systemcomprising a polyol ester or polyvinyl ether refrigerant oil having ananiline point within a range of from −100 to 0° C., the swell of theresin was small with reference to nylon-11 as an example. Further, fromthe results of observation of the circulation state, it was confirmedthat a sufficient circulation amount which is the same as the workingfluid 11 (R-410A) which is a commercially available composition can besecured.

From the above results, it is evident that all the compositions for aheat cycle system comprising each of the working fluids 1 to 10 and 12to 64 and each of the refrigerant oils A, C to D and G to H of thepresent invention are in a favorable circulation state, have excellentproperties also in terms of stability, and are suitable as a compositionfor a heat cycle system.

INDUSTRIAL APPLICABILITY

The composition for a heat cycle system and a heat cycle systememploying the composition of the present invention are useful for arefrigerator (such as a built-in showcase, a separate showcase, anindustrial fridge freezer, a vending machine or an ice making machine),an air-conditioning apparatus (such as a room air-conditioner, a storepackage air-conditioner, a building package air-conditioner, a plantpackage air-conditioner, a gas engine heat pump, a trainair-conditioning system or an automobile air-conditioning system), powergeneration system (such as exhaust heat recovery power generation) or aheat transport apparatus (such as a heat pipe).

This application is a continuation of PCT Application No.PCT/JP2015/054653, filed on Feb. 19, 2015, which is based upon andclaims the benefit of priority from Japanese Patent Application No.2014-030857 filed on Feb. 20, 2014, Japanese Patent Application No.2014-127744 filed on Jun. 20, 2014, Japanese Patent Application No.2014-148347 filed on Jul. 18, 2014 and Japanese Patent Application No.2014-187003 filed on Sep. 12, 2014. The contents of those applicationsare incorporated herein by reference in their entireties.

REFERENCE SYMBOLS

-   -   10: refrigerating cycle system, 11: compressor, 12: condenser,        13: expansion valve, 14: evaporator, 15, 16: pump

What is claimed is:
 1. A composition, comprising a working fluid forheat cycle containing difluoromethane as a saturated fluorinatedhydrocarbon compound, trifluoroethylene and 2,3,3,3-tetrafluoropropeneas unsaturated fluorinated hydrocarbon compounds, and optionally atleast one other unsaturated fluorinated hydrocarbon compound which is acompound comprising at least one carbon-carbon unsaturated bond andrepresented by formula (I), and a refrigerant oil having a breakdownvoltage of at least 25 kV, a hydroxyl value of at most 0.1 mgKOH/g, anda minimum temperature on a high temperature side of a phase separationtemperature from the working fluid for heat cycle of at least 35° C. anda maximum temperature on a low temperature side of at most −60° C.:C_(x)F_(y)R_(z)  (I), where R is H or Cl, x is an integer of from 2 to6, y is an integer of from 1 to 12, and z is an integer of from 0 to 11,provided that 2x≥y+z≥2.
 2. The composition according to claim 1, whereinthe compound of the formula (I) where x is 2 or 3 is contained.
 3. Thecomposition according to claim 2, wherein the at least one otherunsaturated fluorinated hydrocarbon compound selected from the groupconsisting of 1,2-difluoroethylene, 2-fluoropropene,1,1,2-trifluoropropene, (E)-1,2,3,3,3-pentafluoropropene,(Z)-1,2,3,3,3-pentafluoropropene, (E)-1,3,3,3-tetrafluoropropene,(Z)-1,3,3,3-tetrafluoropropene and 3,3,3-trifluoropropene is contained.4. The composition according to claim 1, wherein the working fluid forheat cycle further contains at least one other saturated fluorinatedhydrocarbon compound.
 5. The composition according to claim 4, whereinthe at least one other saturated fluorinated hydrocarbon compoundselected from the group consisting of trifluoromethane, difluoroethane,trifluoroethane, tetrafluoroethane, pentafluoroethane,trifluoroiodomethane, pentafluoropropane, hexafluoropropane,heptafluoropropane, pentafluorobutane and heptafluorocyclopentane iscontained.
 6. The composition according to claim 1, wherein a content oftrifluoroethylene is from 20 to 80 mass % per 100 mass % of the workingfluid.
 7. The composition according to claim 1, wherein a content ofdifluoromethane is from 20 to 80 mass % per 100 mass % of the workingfluid.
 8. The composition according to claim 1, wherein a proportion ofa total amount of trifluoroethylene, 2,3,3,3-tetrafluoropropene anddifluoromethane based on an entire amount of the working fluid is higherthan 90 mass % and at most 100 mass %, and based on the total amount oftrifluoroethylene, 2,3,3,3-tetrafluoropropene and difluoromethane, aproportion of trifluoroethylene is at least 10 mass % and less than 70mass %, a proportion of 2,3,3,3-tetrafluoropropene is higher than 0 mass% and at most 50 mass %, and a proportion of difluoromethane is higherthan 30 mass % and at most 75 mass %.
 9. The composition according toclaim 1, wherein a proportion of a total amount of trifluoroethylene,2,3,3,3-tetrafluoropropene, and difluoromethane based on an entireamount of the working fluid for heat cycle is higher than 90 mass % andat most 100 mass %, based on the total amount of trifluoroethylene,2,3,3,3-tetrafluoropropene, and difluoromethane, a proportion of a totalamount of trifluoroethylene and 2,3,3,3-tetrafluoropropene is at least70 mass %, a proportion of trifluoroethylene is at least 30 mass % andat most 80 mass %, a proportion of 2,3,3,3-tetrafluoropropene is higherthan 0 mass % and at most 40 mass %, and a proportion of difluoromethaneis higher than 0 mass % and at most 30 mass %, and a ratio oftrifluoroethylene to 2,3,3,3-tetrafluoropropene is at most 95/5.
 10. Thecomposition according to claim 1, wherein the refrigerant oil comprisesat least one of a polyol ester refrigerant oil and a polyvinyl etherrefrigerant oil.
 11. The composition according to claim 1, wherein therefrigerant oil has a kinematic viscosity at 40° C. of from 5 to 200mm²/s and a kinematic viscosity at 100° C. of from 1 to 100 mm²/s. 12.The composition according to claim 1, wherein the refrigerant oil has ananiline point of at least −100° C. and at most 0° C.
 13. A heat cyclesystem, comprising the composition according to claim
 1. 14. The heatcycle system according to claim 13, which is at least one of arefrigerating apparatus, an air-conditioning apparatus, a powergeneration system, a heat transport apparatus, and a secondary coolingmachine.
 15. The heat cycle system according to claim 14, whichcomprises a compression mechanism comprising a contact portion incontact with the composition, wherein the contact portion comprises atleast one of an engineering plastic, an organic film, and an inorganicfilm.